Hydraulic fracture composition and method

ABSTRACT

A method for improving the performance of fracturing processes in oil production fields may rely on polymer coated particles carried in the fracturing fluid. The particles may include heavy substrates, such as sand, ceramic sand, or the like coated with polymers selected to absorb water, increasing the area and volume to travel more readily with the flow of fluid without settling out, or allowing the substrate to settle out. Ultimately, the substrate may become lodged in the fissures formed by the pressure or hydraulic fracturing, resulting in propping open of the fissures for improved productivity.

BACKGROUND 1. Related Applications

This application: is a continuation of U.S. patent application Ser. No. 17/202,774, filed Mar. 16, 2021; which is a continuation of U.S. patent application Ser. No. 16/253,934, filed Jan. 22, 2019, now U.S. Pat. No. 10,947,447 issued Mar. 16, 2021; which is a continuation of U.S. patent application Ser. No. 15/416,950, filed Jan. 26, 2017, now abandoned; which is a continuation-in-part of U.S. patent application Ser. No. 15/136,352, filed Apr. 22, 2016, now abandoned; which is a continuation-in-part of U.S. patent application Ser. No. 15/011,111, filed Jan. 29, 2016, now U.S. Pat. No. 9,856,415 issued Jan. 2, 2018; which is a continuation-in-part of U.S. patent application Ser. No. 14/171,920, filed Feb. 4, 2014, now U.S. Pat. No. 10,266,757 issued Apr. 23, 2019; which is a continuation of U.S. patent application Ser. No. 13/418,227, filed Mar. 12, 2012, now U.S. Pat. No. 9,057,014 issued Jun. 16, 2015; which is a continuation-in-part of U.S. patent application Ser. No. 13/299,288, filed Nov. 17, 2011, now U.S. Pat. No. 8,661,729 issued Mar. 4, 2014; which is a continuation-in-part of U.S. patent application Ser. No. 12/789,177, filed May 27, 2010, now U.S. Pat. No. 8,341,881 issued Jan. 1, 2013; which is a continuation of U.S. patent application Ser. No. 12/324,608, filed on Nov. 26, 2008, now U.S. Pat. No. 7,726,070, issued Jun. 1, 2010; which claims the benefit of U.S. provisional patent application Ser. No. 61/012,912, filed Dec. 11, 2007; all of which are hereby incorporated by this reference in their entireties.

2. The Field of the Invention

This invention relates to oil field and oil well development, and, more particularly, to novel systems and methods for fracturing and propping fissures in oil-bearing formations to increase productivity.

3. The Background Art

Oil well development has over one hundred years of extensive engineering and chemical improvements. Various methods for stimulating production of well bores associated with an oil reservoir have been developed. For example, United States Patent Application Publication US 2009/0065253 A1 by Suarez-Rivera et al. and entitled “Method and System for Increasing Production of a Reservoir” is incorporated herein by reference in its entirety and provides a description of fracturing technology in order to increase permeability of reservoirs. Moreover, various techniques exist to further improve the fracture channels, such as by acid etching as described in U.S. Pat. No. 3,943,060, issued Mar. 9, 1976 to Martin et al., which is likewise incorporated herein by reference in its entirety.

In general, different types of processes require various treatments. In general, well production can be improved by fracturing formations. Fracturing is typically done by pumping a formation full of a fluid, containing a large fraction of water, and pressurizing that fluid in order to apply large surface forces to parts of the formation. These large surface forces cause stresses, and by virtue of the massive areas involved, can produce extremely high forces and stresses in the rock formations.

Accordingly, the rock formations tend to shatter, increasing porosity and providing space for the production oil to pass through the formation toward the bore hole for extraction. However, as the foregoing references describe, the chemistry is not simple, the energy and time required for incorporation of various materials into mixtures is time, money, energy, and other resource intensive.

It would be an advance in the art if such properties as viscosity, absorption, mixing, propping, and so forth could be improved by an improved composition and method for introduction.

Moreover, hydraulic fracturing has a rather sophisticated process for adding various constituents to the fracking fluids. Not only must proppants be added, but various other chemicals. In certain fracturing processes, it has been found important or even necessary to blend materials into the working fluid for fracturing. Such blending requires substantial equipment, occupying a very significant footprint on the overall well site.

Moreover, this equipment requires manpower, and maintenance of numerous receiving and storage areas. These are needed for various constituent products that will ultimately be added to the working fluid. All of these processes for mixing auxiliary materials into the fluid cause delays in time, since many of the materials require substantial mixing.

Particularly with small particles, surface tension tends to float such materials on the surface of liquids and require substantial mixing and substantial associated time. Many solids must be pre-mixed in oils, emulsions, and the like, increasing the effect of any spill. Meanwhile, addition of chemicals to a fracturing flow necessarily creates uneven distributions of additives. For example, upon addition, into the flow, a constituent is at a very high concentration near the well head. Meanwhile, none of that newly added constituent exists elsewhere. Thus, the ability to thoroughly distribute material, or to even get it distributed well throughout the fluid being introduced, has proven difficult.

Similarly, transportation of individual constituent chemicals and materials to the well site requires multiple vehicles specialized to different types of materials and phases. For example, some materials are fluids, some are solids, some use a water solvent, some use a petroleum-based solvent, and such materials must be hauled, delivered, and handled in distinct ways with their own suitable storage, handling, and transport equipment.

Various complaints have been encountered with the amount of hydrocarbons, such as various emulsions, chemical additives, including such materials as diesel fuel and the like that are often used. With such liquid chemicals on site, the risk of surface contamination due to chemical spills of such materials is increased. Even when contained in smaller containers, such materials run the risk of spills, carrying about by water, wind, and other weather, as well as the prospect of possible spilling during delivery, handling, or the feeding and mixing processes.

Meanwhile, the operational footprint required for storage, mixing systems, receiving, shipping, and the like increase the overall operational footprint of a well site. Moreover, money, labor, and time are substantial for the process of receiving, preparation, storage, handling, and ultimately mixing materials that will be added to a fracturing fluid.

Thus, it would be a substantial advance in the art to provide a system and method, and particularly a material, that would eliminate many of the handling, equipment, footprint, transportation, and other problems that exist in prior art materials and mixing systems to service fracture fluids.

BRIEF SUMMARY OF THE INVENTION

In view of the foregoing, in accordance with the invention as embodied and broadly described herein, a method, apparatus, and composition are disclosed in certain embodiments in accordance with the present invention, as including a substrate that may be formed of sand, rock product, ceramic sand, gravel, or other hard and structurally strong materials, provided with a binder to temporarily or permanently secure a hydrating polymer in proximity to the substrate. When used herein any reference to sand or proppant refers to any or all of these used in accordance with the invention. In certain embodiments of a method in accordance with the invention, a composition as described may be mixed directly into drilling fluids, such as a fracturing fluid made up of water and other additives.

By virtue of the increased surface area and weight provided to the polymeric powders affixed to the substrate, the surface area, and consequently the frictional drag, is greatly increased, sweeping the material of the invention into a flow of fluid. This greatly decreases the time required to absorb polymers into the fluid.

In fact, rather than having to wait to have the polymers thoroughly mixed, or absorb a full capacity of water, and thereby flow properly with the drilling fluid or fracturing fluid, a composition in accordance with the invention will sweep along with the fluid immediately, with the weight of the substance submerging the polymer. Meanwhile, the cross sectional area presented results in hydrodynamic drag sweeps the composition along with the flow.

Meanwhile, over time, the polymeric powder adhered to the substrate will absorb water, without the necessity for the time, energy, temperature, mixing, and so forth that might otherwise be required by surface mixing. Thus, the composition in accordance with the invention is immediately transportable and flows, relying on the drilling or fracturing fluid as its carrier.

Moreover, as the polymer tends to pick up more water, the density of the granule of substrate and polymer powder becomes closer to the density of water. Accordingly, the size increase and the density change tend to drive the particles of the composition even more homogeneously with the flowing fluid. Thus, the sand does not settle out in various eddies, obstructions, and other locations of low velocity. Rather, the sand continues to be carried with the fluid, providing a double benefit. That is, the sand weight and area helps to initially mix and drive the particles (granules) with the fluid. Thereafter, the hydration of the polymer tends to increase the surface area and reduce the density of the granule or particle, tending to make the particles flow even better and more homogeneously with the surrounding fluid.

Ultimately, as the particles (granules) of the composition flow into fracture locations, they provide very small proppants as the substrates, such as sand, becomes trapped and lodged at various choke points. Nevertheless, because of the small size, the sand or other substrate acting as a proppant, simply needs to provide an offset, keeping fractured surfaces from collapsing back against one another. By providing the small, strong points of separation, the substrate provides a well distributed proppant, carried to maximum extent that the fluids will travel, and deposited in various traps, choke points, and the like.

The net saving in time, money, energy for heating and pumping, and the like is significant. Meanwhile, various technologies for reducing friction in the flow of fluid pumped into bore holes and other formation spaces is described in several patents, including U.S. Pat. No. 3,868,328, issued Feb. 25, 1975 to Boothe et al. and directed to friction reducing compounds, as well as U.S. Pat. No. 3,768,565, issued Oct. 30, 1973 to Persinski et al. and directed to friction reducing, U.S. Patent Application Publication US 2001/0245114 A1 by Gupta et al. directed to well servicing fluid, and U.S. Patent Application Publication US 2008/0064614 A1 by Ahrenst et al. and directed to friction reduction fluids, all described various techniques, materials, methods, and apparatus for developing, implementing, and benefitting from various well fluids. All the foregoing patent application publications and patents are hereby incorporated by reference.

Similarly, the development of various chemicals has been ubiquitous in oil field development. For example, U.S. Pat. No. 3,442,803, issued May 6, 1969 to Hoover et al. is directed to thickened friction reducers, discusses various chemical compositions, and is also incorporated herein by reference in its entirety.

In one embodiment of an apparatus, composition and method in accordance with the invention, a method may be used for formation fracturing. The formation may be in rock and within or near an oil reservoir underground. One may select an oil field region having a formation to be fractured. Fracturing may be sought to increase production. By providing a bore into the formation and a pump, a carrier material, typically comprising a liquid, and sometimes other materials dissolved or carried therein may be pumped into the formation through the bore.

The carrier as a liquid, or slurry comprising a liquid, or otherwise containing a liquid may be driven by the pump to be pressurized into the formation. However, the carrier may be provided an additive formed as granules. Each granule may include a substrate, such as a grain of sand, ceramic sand, crushed rock, other rock products, or the like having bonded thereto many particles (e.g., powder) formed from a polymer.

The polymer may be selected to have various properties, including lubricity, water absorption, water solubility, or the like. This hydrophilic polymer may be bonded permanently, temporarily, or the like to secure to the substrate. Various binders may be used alone or in combination. These may range from a solvent (e.g., organic or water) simply softening the polymer itself to bond it, to glues, sugars, molasses, and various other saccharides, as well as other products, including starches, other polymers, and so forth.

Thus, with some bonds, the polymer powder may be less permanent or attached to have a bond that is less robust. Over time, the polymer powder so attached may wear off, pull away, or otherwise remove from the substrate into the carrier fluid, and may even act as a viscous agent, lubricant, or the like in the carrier.

The method may include introducing the additive directly into the carrier. The more dense substrate will immediately submerge the granules in the carrier at ambient conditions. Thus heating, extensive mixing, waiting, and the like may be dispensed with, as the granules typically will not float or resist mixing once initial surface tension is broken.

Pumping the carrier toward the formation is possible immediately. The carrier fluid carries the granules by the liquid dragging against the substrate, with the particles of polymer attached. The substrate's cross sectional area engages immediately the surrounding liquid, dragging it into the carrier to flow substantially immediately therewith.

Meanwhile, weighting, by the substrate of the polymer, permits the granules to flow into and with the carrier independently from absorption of any of the liquid into the polymer. Nevertheless, over time, absorbing by the polymer a portion of the liquid results in the polymer expanding and providing by the polymer, lubricity to the carrier with respect to the formation.

Creating fractures may be accomplished by pressurizing the carrier in the formation. This creates fissures or fractures. Thus, flowing of the carrier and particles throughout the fractures or fissures in the formation results in lodging, by the particles, within those fractures or fissures. Unable to re-align, adjacent surfaces of rock, now fracture cannot close back together due to propping open the fractures by the substrate granules lodging in the fractures.

The substrate is best if selected from an inorganic material, such as sand, ceramic sand, or other hard, strong, rock product. The polymer may be selected from natural or synthetically formulated polymers. For example polymers of at acrylic acid, acrylate, and various amides are available. Polyacrylamide has been demonstrated suitable for all properties discussed above.

In fracturing a rock formation, the method may include providing an additive comprising a substrate formed as granules, each having an exterior surface, particles formed of a hydrophilic material, the particles being comminuted to a size smaller than the size of the granules and having first and second sides comprising surfaces. The granules may each be coated with the particles, the particles being dry and bonded to the exterior surface by any suitable binder, including the polymer softened with a solvent. The particles are each secured by the first side to the granules, the second side extending radially outward therefrom.

Upon identifying a reservoir, typically far underground from thousands of feet to miles, perhaps, and extending in a formation of rock, one needs to provide a bore into the formation. Providing a carrier, comprising a liquid, and possibly other materials known in the art, is for the purpose of fracturing the formation. Introducing the additive directly into the liquid at ambient conditions is possible, because the substrate weighs the granules down, and there is no need for long mixing, heating or the like as in addition of polymers directly to the carrier.

Thus, pumping may continue or begin immediately to move the carrier and additive down the bore and toward the formation. This results in exposing the second sides of the polymer powder particles directly to the liquid during transit of the carrier and additive toward and into the formation. The polymer particles thus begin absorbing, a portion of the liquid, typically principally water. Swelling of the polymer increases the size, effective diameter, and cross-sectional area, thus increasing the fluid drag on the granules.

Fracturing, typically by hydraulic pressure in the carrier creates fissures in the formation by fracturing the rock pieces in bending, or by layer separation, with tensile stresses breaking the rock. The resulting fissures allow carrying, by the carrier, of the granules into the fissures. However, fissures vary in size and path, resulting in lodging of granules, within the fissures. The granules do not settle out from the carrier, and thus may travel far into the formation and every fissure. However, each time a grain or granule is lodged like a chock stone, it obstructs the ability of the adjacent rock surfaces to close back with one another.

Thus, rather than the proppant (substrate) settling out ineffectually, failing to prop open the fissures, the granules are swept forcefully with the flow of the carrier wherever the carrier can flow, until lodged. Meanwhile, the lubricity of the polymer aids the granules, and thus the substrate from being slowed, trapped, or settled out by the slow flowing boundary layer at the solid wall bounding the flow.

In summary, weighting, by the substrate, sinks the polymer into the carrier readily and independently from absorption of the liquid into the polymer. Mixing, dissolving, and so forth are unnecessary, as the substrate drags the polymer into the carrier, and the carrier drags the granule along with it in its flow path. Lubrication is provided by the polymer between the substrate of each granule and adjacent solid walls of the bore, passages previously existing in the formation, and the fissures formed by fracturing. Any separating, by some of the powdered polymer particles from the substrate, still reduces friction drag on passage of the carrier and particles within the formation.

A composition for fracturing and propping a formation of rock may include a fluid operating as a carrier to be pumped into a rock formation, a substrate comprising granules of an inorganic material, each granule having an outer surface and a size characterized by a maximum dimension thereacross, and all the granules together having an average maximum dimension corresponding thereto. A polymer comprising a hydrophilic material selected to absorb water in an amount greater than the weight thereof may be bound to the substrate. The polymer is comminuted to particles, each particle having a size characterized by a maximum dimension thereacross.

All the polymer particles may be characterized by an average maximum dimension, and an effective (e.g., hydraulic diameter). The average maximum dimension of the particles is best if smaller, preferably much smaller, than the average maximum dimension of the granules.

The particles of the polymer, bound to the substrate, will travel with it in the fluid. Particles of the polymer are thus further directly exposed to water in the fluid during travel with the fluid. The granules, flowing in the fluid, are carried by the hydrodynamic drag of the fluid against the cross-sectional area of the granules coated with the particles of the polymer. The polymer, selected to expand by absorbing water directly from the fluid, increases the area and drag, assisting distribution in the formation by the carrier fluid. The polymer meanwhile operates as a lubricant lubricating the motion of the substrate against the formation during flow of the granules against solid surfaces in the formation, bore, and fracture fissures.

The inorganic material, such as sand, ceramic sand, or the like is typically sized to lodge in fissures formed in the formation and has mechanical properties rendering it a proppant capable of holding open fissures formed in the formation.

In certain embodiments, a water soluble binder is used, then a substrate may release additives into the fracturing fluid quickly or slowly after insertion in the working fluid. A substrate may perform as a proppant, and may be constituted of sand, ceramic, another rock or mineral product, a resin coated, or other material used to prop open fractures. Such a substrate may be provided with a binder securing powdered components of suitable additives to be introduced into a fracturing fluid.

For example, a friction reducer, bioside, oxygen scavenger, clay stabilizer, scale inhibitor, gelling agent, or the like may be included in a mix, or as an element to be adhered to a substrate proppant. The substrate thereby forms particles that will easily be drawn into a flow of fracturing fluid, thus introducing all the necessary constituents into the flow. This occurs rapidly, without having to wait for mixing to occur topside on the site before introduction into the bore. Rather, mixing can take place and hydration or distribution in the flow may take place on the fly as the flow of fluid courses through the bore toward the formation. Thus, the preparation and introduction time on the surface at the well site is minimized.

In certain embodiments, the composition may be mixed directly into the fluid to form a complete and suitable fracturing fluid with all the necessary additives desired. By adhering chemicals to the proppant as the operable substrate, in the correct ratios, elaborate mixing ratios and elaborate mixing processes, and control thereof, as well as their related equipment, personnel, time, storage, and handling are greatly reduced, and optimally eliminated. Thus, the operational footprint of a service company on the well site is reduced, as well as the time, cost, labor, and so forth required to measure, add, mix, and otherwise introduce desired chemical constituents into the fracturing fluid.

By coating a proppant or substrate with the suitable materials (e.g., chemicals, etc.) an even mix of chemicals is maintained within the fracturing fluid much more easily. Moreover, distribution thereof within the flow is straightforward. In fact, all those additives may thereby all be present in exactly the proper ratios at all times at the time they are introduced. Thus, adding them one at a time, working with them to try to get them all introduced at about the same time, and so forth, as encountered in the prior art is no longer a problem.

Because many or all desired constituents may be coated onto a single substrate, or each granule of a single substrate, then numerous constituents, including previously dissolved liquids or solids that have been rendered liquid by introduction into solvents, in order to ensure more rapid mixing, may be reduced or eliminated. Thus the full array of constituent chemicals to be used as additives in the fluid may be provided with proppants in the delivery of a single material, granular in nature, solid in phase, and simple to be stored, transported, handled, and the like. Thus, emissions, spills, other environmental risks, may be reduced or eliminated. By using powdered base chemicals, the carriers or solvents that were previously needed, often hydrocarbon based emulsions and the like, may be eliminated. Thus, the risk of surface spills and consequent contamination may be reduced or eliminated.

In one embodiment, a method for making self-suspending proppant particles is provided. The method includes mixing a volume of substrate particles with a liquid binder so that at least a portion of the volume of substrate particles are at least partly covered with the liquid binder on an outer surface, thereby forming binder-coated substrate particles. The method also includes using a water-in-oil emulsion to apply a first water-absorbing polymer to at least a portion of the binder-coated substrate particles so that the at least a portion of the binder-coated substrate particles are at least partly coated with the first water-absorbing polymer, thereby forming intermediate polymer-coated substrate particles. The method further includes coating at least a portion of the intermediate polymer-coated substrate particles with a second water-absorbing polymer to thereby form polymer coated substrate particles; and drying the polymer coated substrate particles to remove at least a portion of the water-in-oil emulsion to thereby form self-suspending proppant particles. Each of the self-suspending proppant particles are at least partly coated with the second water-absorbing polymer.

In another embodiment, a method for making self-suspending proppant particles is provided. The method includes adding a volume of substrate particles to a mixing vessel, the substrate particles including sand particles. The method also includes applying a first water-absorbing polymer suspended in a liquid to at least a portion of the substrate particles in the mixing vessel, so that the at least a portion of the substrate particles are at least partly coated with the first water-absorbing polymer, thereby forming intermediate polymer-coated substrate particles. The first water-absorbing polymer includes an anionic polyacrylamide. The method further includes coating at least a portion of the intermediate polymer-coated substrate particles with a second water-absorbing polymer in powdered form to thereby form polymer-coated substrate particles; and drying at least a portion of the polymer coated substrate particles to remove at least a portion of the liquid thereby forming self-suspending proppant particles.

In yet another embodiment, self-suspending proppant particles are provided. The self-suspending proppant particles including substrate particles, the substrate particles including sand. The self-suspending proppant particles further including an outer polymeric coating positioned on an outer surface of each of the substrate particles, the outer polymeric coating including at least one water-absorbing polymer in powdered form, where at least a portion of the outer polymeric coating is applied to each of the substrate particles using a water-in-oil emulsion.

In another embodiment, a method for making self-suspending proppant particles is provided. The method includes mixing substrate particles with a liquid binder so that at least a portion of the substrate particles are at least partly coated with the liquid binder. The method also includes applying one or more water-absorbing polymers to the at least a portion of the substrate particles that are at least partly coated with liquid binder to form polymer-coated substrate particles. The applying one or more water-absorbing polymers includes applying a first water-absorbing polymer in a first form, and applying a second water-absorbing polymer in a second form that is different from the first form, where the first and second forms are selected from a powder and an emulsion. Each of the first and second water-absorbing polymers is about 20 mol. % anionic to about 50 mol. % anionic. The method further includes exposing the polymer-coated substrate particles to heat sufficient to cause crosslinking in at least a portion of the one or more water-absorbing polymers present on the polymer coated substrate particles, thereby forming self-suspending proppant particles.

In yet another embodiment, a method for making self-suspending proppant particles is provided. The method includes adding a volume of substrate particles to a mixing vessel, the substrate particles comprising sand. The method also includes coating at least a portion of the substrate particles with glycerol in the mixing vessel to form binder-coated substrate particles. Further, the method includes mixing a first water-absorbing polymer with the binder-coated substrate particles in the mixing vessel. The first water-absorbing polymer includes a co-polymer of acrylamide monomers and acrylate monomers, where the first water-absorbing polymer is about 20 mol. % anionic to about 50 mol. % anionic, and where the first water-absorbing polymer is in powdered form. The method also includes, subsequent to mixing the first water-absorbing polymer with the binder-coated substrate particles, mixing a second water-absorbing polymer with first water-absorbing polymer and the binder-coated substrate particles to form polymer-coated substrate particles. The second water-absorbing polymer including a co-polymer of acrylamide monomers and acrylate monomers, where the second water-absorbing polymer is about 20 mol. % anionic to about 50 mol. % anionic. The second water-absorbing polymer is present in a water-in-oil emulsion, and each of the polymer-coated substrate particles includes a polymeric coating that includes the first water-absorbing polymer and the second water-absorbing polymer. The method further includes exposing the polymer-coated substrate particles to heat sufficient to cause crosslinking in the polymeric coating present on the polymer-coated substrate particles, thereby forming self-suspending proppant particles.

In yet another embodiment, self-suspending proppant particles are provided. The self-suspending proppant particles include substrate particles, the substrate particles including sand. The self-suspending proppant particles further include an outer polymeric coating positioned on an outer surface of each of the substrate particles, the outer polymeric coating including first and second water-absorbing polymers that are at least partly covalently cross-linked. Each of the first and second water-absorbing polymers include a co-polymer of acrylate monomers and acrylamide monomers, where a molecular weight of the first water-absorbing polymer is at least about 1 Million Daltons (g/mol) greater than a molecular weight of the second water-absorbing polymer. Each of the first and second water-absorbing polymers is about 20 mol. % to about 50 mol. % anionic, where the first water-absorbing polymer was applied to the substrate particles in the form of an emulsion, and wherein the second water-absorbing polymer was applied to the substrate particles in powdered form. The self-suspending proppant particles remain suspended in a 1000 ppm CaCO3 aqueous solution for at least 30 minutes at a temperature of 170° F.

BRIEF DESCRIPTION OF THE DRAWINGS

The foregoing features of the present invention will become more fully apparent from the following description and appended claims, taken in conjunction with the accompanying drawings. Understanding that these drawings depict only typical embodiments of the invention and are, therefore, not to be considered limiting of its scope, the invention will be described with additional specificity and detail through use of the accompanying drawings in which:

FIG. 1 is a schematic cross-sectional view of a material including a substrate provided with a binder securing a hydrating polymer thereto in accordance with the invention;

FIG. 2 is a schematic block diagram of one embodiment of a process for formulating and producing fluid additive particles in accordance with the invention;

FIG. 3 is a schematic diagram of the fluid-particle interaction in an apparatus, composition, and method in accordance with the invention;

FIG. 4 is a chart illustrating qualitatively the relationship between volumetric increase over time at various temperatures, illustrating the improved activation with minimum mixing and temperature increase of particles in accordance with the invention;

FIG. 5 is a schematic diagram illustrating one embodiment of friction reducing by polymers used in compositions in accordance with the invention;

FIG. 6A is a schematic diagram of the fracturing and proppant action of particles in accordance with a method and composition according to the invention;

FIG. 6B is a schematic diagram illustrating a collection of proppant particles positioning rock fragments in a formation away from one another in order to maintain open passages in the formation;

FIG. 7 is a schematic block diagram of a fracturing and propping process using compositions and methods in accordance with the invention;

FIG. 8 is a schematic diagram of processes illustrating alternative options for coating, in which particles being adhered to the binder layer may be added sequentially or simultaneously by species or constituent particles;

FIG. 9 is a schematic diagram of an alternative coating process in which multiple binding layers are added over previous binding layers and layers of particles;

FIG. 10 is a schematic block diagram of some alternative coating processes, including direct coating, sequentially adding particular constituents, and sequentially adding binder and particulate constituents to the particles;

FIG. 11 is an image of various self-suspending proppants in the presence of various flowing agents after being exposed to heat and humidity as described in Example 3;

FIG. 12 is an image of the various self-suspending proppants with various flowing agents of FIG. 12 after being exposed to additional heat and humidity as described in Example 3;

FIG. 13A depicts various self-suspending proppants with various flowing agents after being centrifuged and inverted for an initial attempt to remove the proppants from a centrifuge tube as described in Example 3; and

FIG. 13B depicts the self-suspending proppants of FIG. 13A after being removed from the centrifuge tube.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

It will be readily understood that the components of the present invention, as generally described and illustrated in the drawings herein, could be arranged and designed in a wide variety of different configurations. Thus, the following more detailed description of the embodiments of the system and method of the present invention, as represented in the drawings, is not intended to limit the scope of the invention, as claimed, but is merely representative of various embodiments of the invention. The illustrated embodiments of the invention will be best understood by reference to the drawings, wherein like parts are designated by like numerals throughout.

Referring to FIG. 1 , a material 10 in accordance with the invention may include a substrate 12 formed of a suitable material for placement in the vicinity of a fracture region. For example, a substrate may be a particle of sand, ceramic sand, volcanic grit, or other hard material. In some embodiments, a substrate may be formed of organic or inorganic material. Nevertheless, it has been found effective to use sand as a substrate 12 inasmuch as it is submersible in water and will not float as many organic materials will when dry. Likewise, the sand as substrate 12 is comminuted to such a small size that interstices between individual grains of the sand substrate 12 provide ample space and minimum distance for water to surround each of the substrate 12 particles.

In the illustrated embodiment, a binder 14 may be distributed as a comparatively thin layer on the surface of the substrate 12. Typical materials for binders may include both temporary and permanent binders 14. Permanent binders include many polymers, natural and synthetic. Temporary binders may be sugar-based or other water soluble materials. For example, corn syrup, molasses, and the like may form temporary binders. In the presence of water, such material may ultimately dissolve. Nevertheless, so long as the substrate 12 is not turned, mixed, or otherwise disturbed significantly, any other materials supported by the binder 14 would not be expected to dislocate.

Otherwise, certain naturally or synthetically occurring polymers may also be used as a binder 14. Lignicite may be used as a binder 14. Lignicite is a byproduct of wood, and provides material having good adhesive properties, and substantial permanence as a binder 14 on a substrate 12. Any suitable insoluble polymer may be used for more permanent binding.

Other polymers may be used to form a binder 14. For example, various materials used as glues, including mucilage, gelatin, other water soluble polymers including, for example, ELMER'S™ glue, and the like may also operate as binders 14 to bind materials to a substrate 12.

In certain embodiments, the substrate 12 may be used in oil fields as a substrate 12 for polymer additives to fracture fluids. In other situations, the substrate 12 may be implemented as a proppant.

Pigment 16 may be implemented in any of several manners. For example, the substrate 12 may have pigment 16 applied prior to the application of the binder 14. In alternative embodiments, the pigment 16 may actually be included in the binder 14, which becomes a pigmented coating on the substrate 12. In yet other embodiments, the pigments 16 may be added to a hydration particle 18 either as a pigment 16 mixed therein, or as a pigment 16 applied as a coating thereto. Thus the location of the pigment 16 in the Figures is schematic and may take alternative location or application method.

Particles 18 of a hydrophilic polymer material may be bonded to the substrate 12 by the binder 14. Particles may be sized to substantially coat or periodically coat the substrate 12.

In certain embodiments, the hydrophilic material 18 may be a powdered polymeric material 18 such as polyacrylamide or any of the materials in the patent documents incorporated by reference. In other embodiments, the particles 18 may actually be organic material having capillary action to readily absorb and hold water. In one presently contemplated embodiment of an apparatus in accordance with the invention, the particles 18 may be powdered polymeric material in a dehydrated state, and having a capacity to absorb water, typically many times the weight (e.g., five to forty times) of a particular particle 18.

The substrate 12, in certain embodiments, may be some form of sand or granular material. The sand will typically be cleaned and washed to remove dust and organic material that may inhibit the binder 14 from being effective. Likewise, the substrate 12 may be sized of any suitable size. For example, sand particles may range from much less than a millimeter in effective diameter or distance thereacross to approximately two millimeters across. Very coarse sands or ceramic sands may have even larger effective diameters. Hydraulic diameter is effective diameter (four times the area divided by the wetted perimeter). However, in one presently contemplated embodiment, washed and dried sand such as is used in construction, such as in concrete, has been found to be suitable. Fine sands such as masonry sands tend to be smaller, and also can function suitably in accordance with the invention.

Accordingly, the distance across each powder particle 18 may be selected to provide an effective coating of powdered particles 18 on the substrate 12. In one presently contemplated embodiment, the effective diameter of the particles 18 may be from about a 30 mesh size to about a 100 mesh size. For example, a sieve system for classifying particles has various mesh sizes. A size of about 30 mesh, able to pass through a 30 mesh sieve, (i.e., about 0.6 mm) has been found suitable. Likewise, powdering the particles 18 to a size sufficiently small to pass through a 100 mesh (i.e., about 0.015 mm) sieve is also satisfactory. A mesh size of from about 50 mesh to about 75 mesh is an appropriate material to obtain excellent adhesion of particles 18 in the binder 14, with a suitable size of the particles 18 to absorb significant liquid at the surface of the substrate 12.

As a practical matter, about half the volume of a container containing a substrate 12 as particulate matter will be space, interstices between the granules of the substrate 12. One advantage of using materials such as sand as the substrate 12 is that a coating of the particle 18 may provide a substantial volume of water once the particles 18 are fully saturated. By contrast, where the size of the particles 18 is too many orders of magnitude smaller than the effective diameter or size of the substrate particles 12, less of the space between the substrate particles 12 is effectively used for storing water. Thus, sand as a substrate 12 coated by particles 18 of a hydrophilic material such as a polymer will provide substantial space between the substrate particles 12 to hold water-laden particles 18.

The diameter of the particles 18, or the effective diameter thereof, is typically with about an order of magnitude (e.g., 10 x) smaller than the effective diameter of the particles of the substrate 12. This order of magnitude may be changed. For example, the order of magnitude difference less than about 1 order of magnitude (i.e., 10 x) may still be effective. Similarly, an order of magnitude difference of 2 (i.e., 100 x) may also function.

However, with particles 18 too much smaller than an order of magnitude smaller than the effective diameter of the substrate 12, the interstitial space may not be as effectively used. Likewise, with an effective diameter of particles 18 near or larger than about 1 order of magnitude smaller than the size of the particles of the substrate 12, binding may be less effective and the particles 18 may interfere more with the substrate itself as well as the flow of water through the interstitial spaces needed in order to properly hydrate a material 10.

Referring to FIG. 2 , an embodiment of a process for formulating the material 10 may involve cleaning 22 the material of the substrate 12. Likewise, the material of the substrate 12 may be dried 24 to make it more effective in receiving a binder 14. The material of the substrate 12 may then be blended 26.

One embodiment, a ribbon blender provides an effective mechanism to perform continuous blending as the binder 14 is added 28. Other types of mixers, such as rotary mixers, and the like may be used. However, a ribbon blender provides a blending 26 that is effective to distribute binder 14 as it is added 28.

For example, if an individual particle of the substrate 12 receives too much binder 14, and thus begins to agglomerate with other particles of the substrate 12, a ribbon binder will tend to separate the particles as a natural consequences of its shearing and drawing action during blending 26.

As the binder 14 is added 28 to the mixture being blended 26, the individual particles of the substrate 12 will be substantially evenly coated. At this stage, the binder 14 may also be heated in order to reduce its viscosity and improve blending. Likewise, the material of the substrate 12 or the environment of the blending 26 may be heated in order to improve the evenness of the distribution of the binder 14 on the surfaces of the substrate 12 materials or particles 12.

Blending 26 of the binder 14 into the material of the substrate 12 is complete when coating is substantially even, and the texture of the material 10 has an ability to clump, yet is easily crumbled and broken into individual particles. At that point, addition 30 of the hydrophilic particles 18 may be accomplished.

For example, adding 30 the particles 18 as a powder into the blending 26 is a naturally stable process. Typically the particles 18 attach to the binder 14 of the substrate 12 particles, thus removing from activity that location. Accordingly, other particles 18 rather than agglomerating with their own type of material will continue to tumble in the blending 26 until exposed to a suitable location of binder 14 of the substrate 12. Thus, the adding 30 of the particles 18 or powder 18 of hydrophilic material will tend to be a naturally stable process providing a substantially even coating on all the particles of the substrate 12.

Just as marshmallows are dusted with corn starch, rendering them no longer tacky with respect to one another, the material 10 formulated by the process 20 are dusted with particles 18 and will pour freely. Accordingly, distribution 32 may be conducted in a variety of ways and may include one or several processes. For example, distribution may include marketing distribution from packaging after completion of blending 26, shipping to distributers and retailers, and purchase and application by users.

An important part of distribution 32 is the deployment of the material 10. In one embodiment of an apparatus and method in accordance with the invention, the material 10 may be poured, as if it were simply sand 12 or other substrate 12 alone. Since the powder 18 or particles 18 have substantially occupied the binder 14, the material 10 will not bind to itself, but will readily pour as the initial substrate material 12 will.

The material 10 may typically include from about 1 percent to about 20 percent of a hydrophilic material 18 or particles 18. The particles 18 may be formed of a naturally occurring material, such as a cellulose, gelatin, organic material, or the like.

In one embodiment, a synthetic gel, such as polyacrylamide may be used for the particles 18, in a ratio of from about 1 to about 20 percent particles 18 compared to the weight of the substrate 12. In experiments, a range of from about 5 to about 10 percent has been found to be the most effective for the amount particles 18.

Size of particles 18 may range from about 20 mesh to smaller than 100 mesh. Particles 18 of from about 50 to about 75 mesh have been found most effective.

The binder 14 may typically be in the range of from about in ¼ percent to about 3 percent of the weight of the substrate 12. A range of from about ¾ percent to about 1½ percent has been found to work best. That is, with a binder such as lignicite, ¼ of 1 percent has been found not to provide as reliable binding of particles 18 to the substrate 12. Meanwhile, a ratio of higher than about 3 percent by weight of binder 14 to the amount of a substrate 12, such as sand, when using lignicite as the binder 14, tends to provide too much agglomeration. The pouring ability of the material 10 is inhibited as well as the blending 26, due to agglomeration. Other binders also operate, including several smaller molecules that are water soluble. For example, glues, gelatins, sugars, molasses, and the like may be used as a binder 14. Insoluble binders are also useful and more permanent.

One substantial advantage for the material 10 in accordance with the present invention is that the material remains flowable as a sand-like material 10 into the fluids to be used in oil field fracturing. Thus, handling and application is simple, and the ability of granular material 10 to flow under and around small interstices of fractures provides for a very effective application.

Referring to FIG. 3 , a formation 80 such as a reservoir area of an oil may increase large and small flows 82 in passages 84 formed in the rock 86 of the formation 80. Typically, the flow 82 represented by arrows 82 indicating the development of flow at a faster speed in center of a passage 84, and the lower velocity near the wall 88 of the passage 84, illustrates the flow 82 of fluid in the passage 84.

In the illustrated embodiment, the granules 10 or large composite particles 10 or the materials 10 formed as a granulated material 10, having the substrate 12 in the center column with the polymer 18 adhered by a binder 12 on the outside thereof. This material 10 may be added to a flow 82 being pumped into a formation 80. Initially, a particle 10 will have an effective diameter 90 a. In this condition, the particle 10 of material 10 is largely dependent on the density of the substrate 12, which constitutes the majority of its volume. Eventually, over time, with exposure to the liquid 82 or flow 82 and the water of that flow 82, the polymer 18 will absorb water, increasing in its effective diameter 90 b. Ultimately, the polymer 18 or the polymer powder 18 will eventually become fully hydrated, increasing many times its size, and beginning to dominate the effective diameter 90 c or hydraulic diameter 90 c of the particle 10.

Initially, the diameter 90 a reflects the comparatively smaller size and larger density of the particle 10 dominated by the weight of the substrate 12, such as sand, ceramic sand, or some other hard and strong material. Ultimately, the diameter 90 a or effective diameter 90 a is sufficient to provide fluid drag according to fluid dynamic equations, drawing the particle 10 into the flow 82.

Meanwhile, the increase in diameter 90 b and the ultimate effective diameter 90 c result in reduction of the density of the particle 10 as the polymer 18 absorbs more water, bringing the net density of the particle 10 closer to the density of water. Accordingly, the particles 10 flow with the water exactly in sync, so to speak, rather than settling out as a bare substrate 12 would do.

For example, in areas where eddies in the flow occur, such as corners, crevices, walls, and the like, heavy materials having higher density, such as sand and the like, normally will tend to drift out of the flow, toward a wall 88, and ultimately will settle out. Instead, by virtue of the large “sail” presented by the larger diameter 90 c of a fully hydrated polymer 18, each particle 10 stays with the flow 82 in passage 84, providing much more effective transport.

Referring to FIG. 4 , a chart 92 illustrates a volume axis 94 representing the volume of a particle 10 or material 10 in accordance with the invention. The volume axis 94 is displayed orthogonally with respect to a time axis 96, representing the passage of time of the particle 10 submerged in a carrier 82 or flow 82 of fluid 82. Typically, at different temperatures, illustrated by curves 98 a-98 e, with the temperature associated with curve 98 a being the coldest and the temperature associated with the curve 98 e being the hottest, one can visualize how heat added to a fluid flow 82 tends to increase the chemical activity and thus the rate of absorption of water into a polymer 18.

In an apparatus and method in accordance with the invention, the particles 10 may be added directly to a flow 82, without waiting for any significant time to absorb water into the polymer 18. Instead, the normal flow 82 will draw the particles 10 along in a passage 84 while exposing each individual particle 10 to surrounding fluid 82, thus promoting maximum rates of exposure and increased rates of absorption. Accordingly, the volume 94 increases, representing an increase in the absorption of water into the polymer 18.

In an apparatus and method in accordance with the invention, the curve 98 a is suitable because the entire travel within the well bore, and with the formation 80 by the fluid 82 bearing the particles 10 is permissible and available as absorption time. By contrast, prior art systems rely on the increased temperature of curve 98 e in order to provide the time, temperature, and mixing to work polymers into a flow 82 or liquid carrier 82.

Referring to FIG. 5 , in one embodiment of an apparatus, composition, and method in accordance with the invention, some of the polymer 18 may eventually be scraped, sheared, or otherwise removed from the particles 10. If bonded only by itself with a water solvent, such a separation may be easier than if bonded by a more durable polymer. Such a release may even be engineered, timed, controlled by a solvent, or the like.

Thus, a certain amount of the polymer 18 may be released from the granule 10 into the carrier fluid 82 to flow with the fluid 82 and operate as a general friction reducer or provide its other inherent properties to the carrier fluid 82. By an engineered process of bonding and un-bonding, the polymer powder may be less permanent or attached to have a bond that is less robust. Over time, the polymer powder so attached may release, tear, wear off, pull away, or otherwise remove from the substrate into the carrier fluid to act as a viscosity agent, surfactant, lubricant, or the like in the carrier, according to its known properties available for modifying the carrier 82.

For example, a polymer 100 or polymer chain 100 may be captured on a corner 102 defining a passage 84 into which a flow 82 will proceed. Accordingly, the corner 102 renders less of an orifice on the passage 84 against entry of the flow 82 by virtue of the friction reduction of the polymer 100 in the fluid, deposited temporarily or permanently about a corner 102. Thus, other particles 10 passing the corner 100 may shear off a portion of the polymer 18 carried thereby or may rely on the presence of the polymer 18 as a direct friction reducing agent on the particle 10 (granule) itself, permitting the particles 10 to pass more easily with the flow 82 into the passage 84.

Referring to FIGS. 6A and 6B, various fracture processes are described in various literature, including U.S. Patent Application publication US 2009/0065253 by Suarez-Rivera et al. incorporated herein by reference. In a fracturing process, the pressure 110 or force 110 applied to a formation 80 tends to force apart large expanses of rock. As a result of that expansion of passages 84 in a rock formation 80, the rock is stressed. Pressure pumped into the fluid 82 flowing in the passages 84 within the formation 80 results in bending stresses, tensile stresses, and so forth in the formation 80.

In FIG. 6A, the forces 110 illustrated the effect of a large pressure applied over a large area. Since pressure multiplied by area equals force, applying an elevated hydraulic pressure to a large surface of a rock 86 or rock segment 86 within a formation 80 results in tensile forces. Compressive forces will not tend to break rock. However, a tensile force, which may be induced by bending, expansion, or the like, results in fracture of the rock. The fracture of the rock 86 thus results in condition shown in the lower view, in which the passages 84 are mere fissures within the rock 86.

The inset of FIG. 6A magnifies the fissures 84 or passages 84 formed in the rock 86 and immediately entered by the working fluid 82 being used for the fracture. Having the particles 10 formed around substrates 12, the fluid 82 extends into each of the fissures formed. Fissures 84 are simply passages 84. Some may be large, others small.

Referring to FIG. 6B, proppants 10 trapped in a small location still displace a large amount of fractured rock 86. Thus, a small displacement at one location may still maintain opened another opening much larger elsewhere near the rock 86. The particles 10, even if as small as sand, may also collect and fill larger dead ends, slow flowing, and eddying spaces, eliminating the ability for rocks 86 to return to former positions.

After fracturing rock 86 to form all of the fissures 84, the fluid 82 will pass through the fissures, carrying particles 10, which eventually collect in cavities or reach choke points. In the absence of the particles 10, fissures 84 could close back up after the fracturing water leaves. However, by containing additives 18, and then losing them, the individual substrates 12 are themselves rock in the form of sand, ceramic sand, or the like. Thus, a particle 10 or many particles 10 need only obstruct the ability of the fissure 84 to close, and may “prop” open the fissures 84 precluding the rock 86 or the pieces of rock 86 from settling back into alignment with one another.

Thus, the particles 10 both alone and in collected piles act as proppants left behind by the fluid flow 82, by virtue of the particles 10 b captured. As a practical matter, it is the substrate 12 that acts as a proppant. The polymers 18 may eventually be worn off, or released by a water-soluble binder, but can easily be compressed, distorted, or cut. Regardless, as the fissures 84 open, they are back filled and close in at choke points and settling points collecting the substrate 12.

Continuing to refer to FIG. 6B, while referring generally to FIGS. 1-10 , a formation 80 when fractured into individual pieces of stone 86, may form various passages 84 or fissures 84 therein. To the extent that proppant materials 10 lose the adhered particles 18 or powders 18, once hydrated or mixed into the fluid 82, the substrate 12 is then in a position to be deposited by eddies, slower flows, turning corners, and the like. Thus, when the other materials 18 that have acted sails, drifting the substrate 12 with the fluid 82, have been removed, then the substrate 12 can more easily settle out. Accordingly, near corners, in small crevices, in dead corners, and the like, the particles 10, largely stripped of their added constituent powders 18 (in whatever phase at that point) may then drop out of the fluid 82 in a slow flow.

Once two portions of rock 86 separate from one another, forming a passage 84 of some size, a supply of proppant 10 b may then prevent that rock portion 86 from moving back into its exact position, necessarily forming passages 84 on virtually every side. Where a single particle 10 of substrate 12 may drop out of the fluid 82 and collect, many more may likewise collect. Accordingly, the various particles 10 b illustrated in FIG. 6B may collect, forming substantial support for various edges, corners, and the like of various rock 86. The result is that a small material, in comparatively small quantities, supporting an edge, or a particular region of a rock 86 in the formation 80 may nevertheless maintain a large network of passages 84 as a direct result.

In stone formations having stronger tensile strength, fractures may produce less debris to act as natural proppants. Nevertheless, in addition to the particles 10 constituting primarily substrate material 12 at this point, the passages 84 may be maintained open as is the objective with fracturing.

Referring to FIG. 7 , a process 111 may include preparing 112 a fluid 82. Processing 114 other additives other than the particles 10 may be done according to any suitable methods, including prior art processes. Adding 116 directly to the fluid 82, the particles 10 as described hereinabove, may be done in such a manner that the operators need not wait for absorption or any other processes to take place. Additional energy for elevating temperature is not required, neither mixing or the like, other than adding 116 directly particles 10 into the flow 82. The flow 82 will immediately grab the particles 10 according to the principles of fluid dynamics in which fluid drag is dependent upon a shape factor of the particle 10, the density of the fluid 82, the square of velocity of the fluid, and so forth, as defined in engineering fluid mechanics.

The fluid 82 now bearing the particles 10 would be immediately pumped 118 into the formation 80 that is the reservoir 80 of an oil field. Eventually, pressurizing 120 the reservoir by pressurizing the fluid 82 results in creating 122 fractures 84 or fissures 84 within the formation 80 by breaking up the rock 86 of the formation 80. A fracture 84 with enough displacement may make a site for material 10 to stagnate and collect.

Creating 122 fracture lines throughout the formation 80 is followed by penetrating 124, by the particles 10 borne in the fluid 82 into the passages 84 or fissures 84 in the rock 86 of the formation 80. Whenever the flow 82 of fluid 82 carries a particle 10 to a choke point 108 in a passage 84, as illustrated in FIG. 6 , a particle 10 will be lodged as illustrated in the insert of FIG. 6 , a particle 10 with its polymer 18 still secured and intact may be lodged. Similarly, the substrate 12 may be lodged 126 and the polymer 18 may be stripped therefrom by the consequent or subsequent flowing of material in the flow 82. Likewise, piles of stagnant particles 10 may backfill spaces, precluding rock 86 settling back in.

After the lodging 126 or propping 126 of the fissures 84 by the substrate 12, in the particles 10, the passages 84 will remain open. These fissures 84 may then be used to later withdraw 128 the fluid 82 from the formation 80. Thereafter, returning 130 the formation 80 to production may occur in any manner suitable. For example, heat may be added to the formation, liquid may be run through the formation as a driver to push petroleum out, or the like.

Referring to FIGS. 8-10 , while continuing to refer generally to FIGS. 1-10 , in various alternative embodiments, multiple constituents may be used as the particles 18 or powder 18 held by the binder 14 to the substrate 12. For example, in various alternative embodiments, one or more other constituents may be added in addition to friction reducers. In the embodiments described hereinabove, the polymeric powders 18 added to the substrate 12 by the tacky or otherwise adhering binder material 14 operated partly as a friction reducer but also as a sill encouraging drifting of the particles 10 with the flow of the fluid 82 or flow 82 in the fracture fluid 82. Thus, hydrophilic powder 18 served multiple purposes.

Meanwhile, as described hereinabove, such polymers may be bonded to the outer surface of the binder 14, thus rendering themselves more susceptible to absorbing water and being stripped off by friction against the walls 88 of various passages 84 in the formation 80. Accordingly, such materials may typically be used in combination with others in various fractures. It has been found effective to include a friction reducing material at a fraction of about 0 to about 10 percent of the total coating granules 18 or powder 18 adhered to the binder 14.

Similarly, biological organisms can change the pH in the water 82 or fluid 82 used for the fracture process. Accordingly, biocides or bacteriacides may eliminate the bacteria or reduce its population in order to avoid changes in the mechanical properties of the fluid 82 as well as changing the pH and thereby the corrosiveness of the fluid 82.

In the contemplated embodiment, such materials such as sodium hypochlorite as a powder or crystal form may be used as one of the constituents for the powder 18 to be bound by the binder 14. Likewise, chlorine dioxide may also be applied by a powder formed of a crystal and form thereof. Other biocides that may be included may be glutaraldehyde as a liquid, or as the constituents thereof in solid form. Similarly, quaternary ammonium chloride may be provided as a solid and therefore as a powder, or as a liquid.

Liquids may be included in the binder 14. Alternatively, the liquid constituents may instead by separated from (or not dissolved in) their solvents in order to provide powders 18 for adhering to the particles 10. Thus, the foregoing liquids as well as tetrakis hydroxhydroxymethyl-phosphonium sulfate may be similarly treated.

As one or even as the only constituent, a particular material may be used as powder 18 adhered to the substrate 12 as part of a particle 10. Any one or more may be combined appropriately. Biocides, typically appear to be suitable in the range of from about 0 to about 3 percent of the particles 18 or powder 18 secured to the substrate 12.

Oxygen scavengers also assist in changing pH as well as preventing corrosion, by removing available oxygen from the fluid 82. Removal of oxygen prevents oxidation, commonly known as rust or corrosion. Thus, the liners, drilling equipment, and other tubular materials may increase their life and reliability and overall integrity of the well by reducing oxygen in the fluid 82. Accordingly, from about 0 to about 3 percent of an oxygen scavenger may be included as part of the coating 18 or the powder 18 adhered to each substrate 12.

Similarly, a clay stabilizer may be included in a proportion of from about 0 to about 3 percent of the coating 18. Thus, clay stabilizers that are used in the fluid 82 may be modified or restricted from swelling or shifting. For example, choline chloride as well as tetramethyl ammonium chloride as well as sodium chloride (salt) may all be provided as powders 18 to be bonded to the substrate 12 by a binder 14.

Likewise, scaling inhibitors may be included at a rate of from about 0 to about 3 percent of the powder 18 adhered to the substrate 12 or of the total weight of the product. Scaling involves the deposition on various conduits and walls, typically in pipes of various minerals, such as carbonates. Changes in pH, changes in temperature, changes in various concentrations of other materials including that of the scaling material may cause scale to accumulate. Accordingly, scale inhibitors may be added as particles 18 in an overall mix, or as part of another coating process.

For example, various copolymers of acrylamides as well as sodium acrylate are scale inhibitors that may be secured to the substrate 12 by the binder 14. Similarly, sodium polycarboxylate and phosphonic acid salt may all be provided in a solid form. All may be comminuted to a powder 18, and sieved to a common size corresponding to that of other materials. Accordingly, mixed in a proper ratio, the powders 18 may actually be compositions of numerous constituents in suitable proportions.

Likewise, a gelling agent may be added in a proportion of from about 0 to about 10 percent as a powder 18 secured to the substrate 12 of particle 10. A function of gelling agents is to alter viscosity. This improves suspension of proppants, such as the substrate 12, sand, or the like, in water. Typically, the speed or velocity with which gravity or other effects may drift a heavy substrate 12 or particle 10 out of solution to leave it elsewhere, is controlled to a large extent by the relative viscosity of the liquid fluid 82 through which the particles 10 are passing. Accordingly, increasing the viscosity tends to keep the particles 10 entrained and more evenly distributed within the fluid 82.

Accordingly, various gelling agents, or a single gelling agent selection may be used as a constituent forming the powder 18 adhered to a substrate 12. Typical processes describe hereinabove and hereinafter illustrate that solid particles may be inducted into the flow 82 or the fluid 82 almost instantly when introduced as the particulates 10. Thus, rather than floating on top during extensive mixing, such materials may be drawn quickly as part of the particles 10 discharged into the fluid 82 at the well head.

Various experiments have shown the utility and ability to add many of these materials. Generally, anything that can be maintained stable for a suitable period of time may be added as powder 18 to a suitable binder 14 holding it to a substrate 12. Thus, various hydrophilic polymers, including polyacrylamides and polyacrylates may be added. Guar gum, various guar derivatives, polysaccharide blends all have the mechanical properties to be suitable as constituents of the powder 18 of particles 10.

Referring to FIG. 8 , in one embodiment of a process in accordance with the invention, a substrate 12 may have added to it a layer of binder 14. To the binder 14 may be added a particular powder 18 a or additive 18 a in solid form to be bound to the substrate 12 by the binder 14. In this particular embodiment, the powder 18 a is added first, in a particular fraction. Thereafter, various other constituents may be added in series as the powders 18 b, 18 c, 18 d, illustrated by differing shapes of particles. For example, the particles or powder 18 a is illustrated by an irregular shape, the powder 18 b by a rectangular shape, 18 c by a diamond shape, and 18 d by a circular shape. These shapes are merely schematic in order to show the addition of various materials.

Continuing to refer to FIG. 8 , the process may also operate by a method of first mixing each of the different powders 18, including up to about 10 or more. Typically, additives in the range of from about 5 to about 9 different constituents may be comminuted and sieved (sorted) in order to maintain all at approximately the same range of sizes.

In this way, by grinding to powder (comminuting) and then sorting with a sieve, the various constituent materials may then be treated mechanically as generic materials, mechanically equivalent. Thus, all may be mixed together.

An important feature here is to avoid disparate sizes, and particularly the inclusions of too many fines. Ultra fine particles tend to provide less included volume in each powder particle, and thus occupy more surface of the available binder 14 and the surface area of the substrate 12, thus inhibiting even coating and the addition of other constituents. Thus, in such an embodiment, the powder particles 18 a, 18 b, 18 c, 18 d, and so forth may all be mixed in the exact proportion desired, usually as a fraction or percentage of the total weight of particles 10, and each may then be included in a mixed supply (e.g., bin, etc.) having the proportions desired, of each and every constituent. Thus, the process described with respect to FIGS. 1 and 2 hereinabove may be used directly, with the powder 18 simply being a mix of other individual constituent chemicals as powders. Thus, all constituents may be added “in parallel,” simultaneously.

Referring to FIG. 9 , in an alternative embodiment, the substrate 12 may have added to it a binder 14, after which a layer of particles 18 may be added to the binder. Following this, an additional layer of binder 14 may be added to which additional particles 18 may be adhered.

In this embodiment, the additional layers of binder 14 and particles 18 may provide sequential de-layering of the various powders 18 during the process of flowing through the bore and into the formation 80. Nevertheless, it has been found that adhering a supply of particles 18 or powder 18 to a single layer of binder 14, provides adequate surface area, adequate binding, and sufficient area to hold a wide variety of constituent chemicals all adhered in a single coating process.

Referring to FIG. 10 , while continuing to refer generally to FIGS. 1-10 , one embodiment of a process 20 may be illustrated with the cleaning 22, drying 24, and blending 26 as described hereinabove. Meanwhile, a decision 132 determines the mode of coating. For example, if the decision is to coat directly, then preparing 134 sieved constituents may include comminuting and sorting constituents, each sieved or otherwise sorted in order to provide a consistent size range for each.

Following the preparation 134 of the constituents, mixing 136 is needed for the constituents in the suitable ratios or percentages. This provides a single mixture of powdered particles 18 suitable for bonding to a substrate 12. Applying 138 a binder is followed by applying 140 the powder 18 to the binder 14 in coating the substrate 12 as described hereinabove.

Following preparation of the granular particulates 10, postprocessing may include bagging, may include additional drying, or may include protection against elements to which the material 10 will be exposed.

Post processing 142 may be followed by distribution 144 to various destinations. Distribution 144 may include, or may be followed up by stocking the distributed 144 product 10 at various sites for use. Ultimately, injecting 148 the granular material 10 into the fluid 82 for fracturing may complete the preparation and use of the product 10 in accordance with the invention. Thereafter, the processes described with respect to FIGS. 3-6B occur as a consequence of the configuration of the granular material 10.

In certain alternative embodiments, as illustrated in FIGS. 8 and 9 , the mode decision 132 may involve adding powder 18 in series. For example, adding 150 a binder may be followed by adding 152 a powder species. Thereafter, a decision 154 may determine whether to add another species. If the decision is affirmative, then additional species may be added 152 until the coating is completed. Thereafter, when no other additions are to be made, according to the decision step 154, then postprocessing 142 continues, and the process 20 continues to ejection 148.

Similarly, the process of FIG. 9 illustrates the process in which adding 160 a binder 14 is followed by adding 162 a powder constituent, after which a decision 164 results in adding 160 more binder before adding 162 more of a powder constituent. Thus, adding 152 powder only, compared to adding 168 binder 14 and adding 162 additional powdered constituents 18, reflect certain of the embodiments such as FIG. 9 . Nevertheless, the embodiment of preparing 134 sieved constituents, through the applying 140 the powder 18 as a mixture, is also illustrated in FIG. 8 , or represented thereby, as described hereinabove.

As discussed above, the material 10 may be utilized as self-suspending proppants in hydraulic fracturing. As used herein, the material 10 may also be referred to as self-suspending proppants.

Methods for Forming Self-Suspending Proppant Particles

In various embodiments, as discussed above, the self-suspending proppants described herein may include a substrate, e.g., sand, having an outer polymeric coating that is water-absorbing. In such embodiments, a water-absorbing outer polymeric coating comprises one or more water-absorbing polymers, such as the water-absorbing polymers discussed below. In addition, in various embodiments, as discussed above, the self-suspending proppants may include a binder, which may aid in securing at least a portion of the water-absorbing polymeric coating to the substrate.

In certain embodiments, the substrate can include frac sand. In one or more embodiments, the frac sand can be graded as a 12-20 mesh frac sand, a 16-30 mesh frac sand, a 20-40 mesh frac sand, a 30-50 mesh frac sand, a 30-70 mesh frac sand, a 40-70 mesh frac sand, or a 100+ mesh frac sand. In certain embodiments, a combination of various grades of frac sand can be used, such as a combination of the grades listed above. Such frac sands and grades are commercially available.

Methods for Forming Self-Suspending Proppant Particles: Binder-Coated Substrate Particles

In embodiments, as discussed above, the self-suspending proppant can be made by first mixing a substrate with a binder to form binder-coated substrate particles. In certain embodiments, the binder may be a liquid binder, such as glycerol. Other liquid binders are described above.

In one or more embodiments, when mixing a binder with a substrate, one may add at least about 0.05 wt. % binder, at least about 0.1 wt. % binder, at least about 0.15 wt. % binder, or at least about 0.2 wt. % binder; and/or less than about 3 wt. % binder, less than about 2 wt. % binder, less than about 1 wt. % binder, or less than about 0.5 wt. % binder. In the same or alternative embodiments, when mixing a binder with a substrate, one may add about 0.25 wt. % binder. As used herein, “wt. % binder” refers to the ratio of the weight of the binder to the weight of the substrate, multiplies by 100.

In embodiments, the binder and substrate can be mixed using any commercially available mixing device or mixing vessel and a particular one can be chosen by one skilled in the art for a specific purpose. In certain embodiments, a ribbon mixer or paddle mixer may be utilized when mixing the binder and substrate.

In certain embodiments, the binder and substrate may be mixed for a time sufficient to substantially evenly apply the binder to the substrate particles. In one or more embodiments, the binder may be mixed with the substrate for at least about 1-2 minutes. In certain embodiments, upon mixing the binder and substrate under the conditions described herein, a substantial portion, or substantially all of, the binder may be coated onto the outer surface of the substrate particles so that there is little to no excess free binder.

Methods for Forming Self-Suspending Proppant Particles: Intermediate Polymer-Coated Substrate Particles

In embodiments, at least a portion of the binder-coated substrate particles, or substrate particles without binder, may be coated with one or more polymeric materials, such as water-absorbing polymers to form intermediate polymer-coated substrate particles. In one or more embodiments, the water-absorbing polymers utilized to form the intermediate polymer-coated substrate particles can include polyacrylamide, polyacrylates, or a combination thereof. In certain embodiments, the water absorbing polymers can include a co-polymer of acrylamide monomers and acrylate monomers. In such embodiments, the co-polymer of acrylamide monomers and acrylate monomers may be a random co-polymer of acrylate monomers and acrylamide monomers such that the acrylate monomers and the acrylamide monomers are randomly positioned within the co-polymer.

In embodiments, any of the water-absorbing polymers disclosed herein may be linear or cross-linked. As used herein, a polymer that is linear refers to a polymer that is not cross-linked with itself or another polymer by covalent bonds and/or ionic bonds. In certain embodiments, a polymer that is linear, while not being cross-linked, can include simple linear polymers and branched linear polymers. A simple linear polymer refers to a polymer having a single long chain, while a branched linear polymer refers to a polymer having a long chain with one or more shorter chains branched off from the long chain.

In certain embodiments, the water-absorbing polymer can include an anionic polymer, such as polyacrylamide or a co-polymer of acrylate monomers and acrylamide monomers. As discussed above, the polyacrylamide can include a linear polyacrylamide. In various embodiments, the anionic polyacrylamide or other anionic polymer, such as an anionic co-polymer of acrylamide monomers and acrylate monomers, can have an anionic charge in an amount of about 10 mol %, about 20 mol %, about 30 mol %, about 40 mol % or about 50 mol %. In embodiments, the anionic polymer or co-polymer can be about 10 mol % to about 50 mol % anionic, about 20 mol % to about 50 mol % anionic, or about 30 mol % to about 40 mol % anionic. In certain embodiments, within an anionic co-polymer of acrylate monomers and acrylamide monomers, the anionic content may substantially correlate to the content of the acrylate monomers in the co-polymer. For instance, in such embodiments, a co-polymer of acrylate monomers and acrylamide monomers that is about 20 mol % to 50 mol % anionic, can include about 20 mol % to about 50 mol % acrylate monomers.

In various embodiments, a co-polymer of acrylate monomers and acrylamide monomers may include neutral or non-ionic acrylamide monomers and anionic acrylate monomers. In such embodiments, the acrylamide monomers can be present in the co-polymer in an amount of at least about 50 mol %, at least about 60 mol %, at least about 70 mol %, or at least about 90 mol %; or from about 40 mol % to about 90 mol %, or from about 50 mol % to about 90 mol %, or from about 50 mol % to about 80 mol %. In the same or alternative embodiments, the water-absorbing polymer can include a non-ionic polymer, cationic polymer, anionic polymer, or a combination thereof. It is appreciated that one skilled in the art is aware that such types of water-absorbing polymers can be commercially obtained. Representative commercial vendors includes SNF and Evonik.

In certain embodiments, utilizing water-absorbing polymers having the anionic content ranges described above can provide some advantageous functional properties to the self-suspending proppants. For example, in certain embodiments, utilizing water-absorbing polymers having the anionic content ranges described above can result in the effective suspension of the self-suspending proppants in an aqueous fluid, including brackish water. Further, in certain embodiments, the anionic content of a water-absorbing polymer described herein may affect the molecular weight or size of the polymer, which may affect the ability of the polymer to form a polymer coating on the substrate particle. In such an embodiment, utilizing water-absorbing polymers having the anionic content ranges described above allows for the appropriate molecular weight of the water-absorbing polymer so that such a polymer can form an effective polymer coating on the substrate particles. These and other properties are discussed further below.

In embodiments, the water-absorbing polymer can have a molecular weight of at least about 1 million Daltons (g/mol), at least about 5 million Daltons (g/mol), at least about 15 million Daltons (g/mol), or at least about 20 million Daltons (g/mol). In the same or alternative embodiments, the water-absorbing polymer can have a molecular weight of about 40 million Daltons (g/mol) or less, or about 30 million Daltons (g/mol) or less.

In certain embodiments, coating the binder-coated substrate particles with one or more polymeric materials to form intermediate polymer-coated substrate particles can include applying one or more polymeric materials to a mixing vessel or device containing binder-coated substrate particles, such as the mixing devices discussed above.

In certain embodiments, the water-absorbing polymers may be suspending in liquid prior to being added to a mixing vessel containing the substrate particles or binder-coated substrate particles. In one or more embodiments, the water-absorbing polymer may be present in a water-in-oil emulsion (i.e., an invert emulsion). In such embodiments, the water-in-oil emulsion may include the water-absorbing polymer in the water or aqueous phase, which is emulsified in the larger oil phase, such as a mineral oil or other distillates of petroleum. In addition, in such embodiments, the water-absorbing polymer may be present in the water-in-oil emulsion in an amount of about 15 wt. %, about 20 wt. %, about 25 wt. %, about 30 wt. %, about 40 wt. %, or about 50 wt. %. It is appreciated that one skilled in the art understands that water-in-oil emulsions comprising water-absorbing polymers can be commercially obtained. One such commercial vendor is SNF.

In one or more embodiments, when a water-in-oil emulsion is utilized, the emulsion can be added to the binder-coated substrate, or plain substrate, in an amount of at least about 0.1 wt. % emulsion relative to the weight of the substrate, at least about 0.2 wt. %, at least about 0.3 wt. %, at least about 0.4 wt. %, at least about 0.5 wt. %, at least about 1 wt. %, at least about 2 wt. %, at least about 2.5 wt. %, at least about 3 wt. %, at least about 4 wt. %, at least about 5 wt. %, or at least about 7.5 wt. %. In the same or alternative embodiments, the emulsion can be added to the binder-coated substrate, or plain substrate, in an amount of less than about 20 wt. % emulsion relative to the weight of the substrate, less than about 15 wt. %, or less than about 10 wt. %. As used herein, “wt. % emulsion relative to the weight of the substrate” refers to the ratio of the weight of the emulsion to the weight of the substrate, multiplied by 100.

In certain embodiments, the water-absorbing polymer may be mixed with the binder-coated substrate particles, or substrate particles, for a time sufficient to substantially evenly apply the water-absorbing polymer, or the liquid or emulsion containing the water-absorbing polymer, to the substrate particles to form the intermediate polymer-coated substrate particles. In one or more embodiments, the intermediate polymer-coated substrate particles can be fully coated with water-absorbing polymer and/or the liquid or emulsion containing the water-absorbing polymer. In one or more embodiments, the water absorbing polymer may be mixed with the substrate for about 1-0 minutes, or about 2-3 minutes.

Without being bound by any particular theories, in certain embodiments, it is believed that the humectant properties of the binder, such as the humectant properties of glycerol, may attract the aqueous dispersion of water-absorbing polymer from the water-in-oil emulsion to the surface of the substrate particles resulting in the coating of the water-absorbing polymer onto the surface of the substrate particle. In such embodiments, the binder can include other humectants or hygroscopic compounds known to one skilled in the art.

In alternative embodiments, the water-absorbing polymers may be in dried powdered form prior to being added to a mixing vessel containing the substrate particles or binder-coated substrate particles. The dried powdered form of the water-absorbing polymers can include any or all of the features of the dried powdered form of water-absorbing polymers discussed below. For instance, the water-absorbing polymer in dried powdered form can include powder particles of less than about 300 microns, less than about 200 microns, or less than about 100 microns. In one or more embodiments, the water-absorbing polymer in dried powdered form can include powder particles with a maximum dimension of less than about 300 microns, less than about 200 microns, or less than about 100 microns. In the same or alternative embodiments, a water-absorbing polymer in powdered form refers to a dry powdered polymer having a dry content of: at least about 50%, at least about 75%, at least about 85%, at least about 95%, or at least about 99%; or a dry content of from about 75%-100% or about 88%-100%.

In embodiments when the dried powdered form of the water-absorbing polymer is added to a mixing vessel containing the substrate particles or binder-coated substrate particles to form intermediate-coated substrate particles, the water-absorbing polymer can be added in an amount of 0.01 wt. % water-absorbing polymer relative to the weight of the substrate, at least about 0.1 wt. %, at least about 0.25 wt. %, at least about 0.5 wt. %, at least about 1 wt. %, at least about 1.5 wt. %, or at least about 2 wt. %, and/or less than about 10 wt. %, less than about 7.5 wt. %, less than about 5 wt. %, or less than about 3 wt. %.

Methods for Forming Self-Suspending Proppant Particles: Polymer-Coated Substrate Particles

In various embodiments, the intermediate polymer-coated substrate particles can be coated with a second water-absorbing polymer to form polymer-coated substrate particles. In certain embodiments, the second water absorbing polymer can have any or all of the parameters and properties of the water-absorbing polymers described above. In various embodiments, the water-absorbing polymer applied to the intermediate polymer-coated substrate particles can include an acrylamide and acrylate co-polymer that is cross-linked. In various other embodiments, the water-absorbing polymer applied to the intermediate polymer-coated substrate can include a linear co-polymer of acrylate monomers and acrylamide monomers. In the same or alternative embodiments, the water-absorbing polymer applied to the intermediate polymer-coated substrate particles can include a linear polyacrylamide. In such embodiments, the linear polyacrylamide applied at this step may have an increased molecular weight relative to the water-absorbing polymer applied in forming the intermediate polymer-coated substrate particles.

In certain embodiments, a water-absorbing polymer utilized in an emulsion can have a greater molecular weight than a water-absorbing polymer utilized in powdered form. In such embodiments, the molecular weight of the water-absorbing polymer present in an emulsion can be at least about 1 million Daltons (g/mol), at least about 2 million Daltons (g/mol), or at least about 3 million Daltons (g/mol) greater than the molecular weight of the water-absorbing polymer present in powdered form.

In one or more embodiments, the polymer coated substrate particles can be formed by applying the second water-absorbing polymer to the intermediate polymer-coated substrate particles in a mixing vessel, such as the mixing vessels discussed above.

In certain embodiments, the second water-absorbing polymer may be present in powdered form when applying to the intermediate polymer-coated substrate particles. In certain embodiments, a water-absorbing polymer in powdered form refers to a dry powdered polymer with powder particles of less than about 300 microns, less than about 200 microns, or less than about 100 microns. In the same or alternative embodiments, a water-absorbing polymer in powdered form refers to a dry powdered polymer having a dry content of: at least 50%, at least about 75%, at least about 85%, at least about 95%, or at least about 99%; or a dry content of from about 75%-100% or about 88%-100%. In embodiments, the processes described above for forming the intermediate polymer-coated substrate particles may result in the intermediate polymer-coated substrate particles having an outer wet surface, due to the application of the binder and/or the application of a water absorbing polymer in a liquid, such as an emulsion described above. In such embodiments, a dry powdered second water-absorbing polymer may adhere to the wet outer surface of the intermediate polymer-coated substrate particles.

In one or more embodiments, the second water-absorbing polymer may be applied in an amount so as to not completely, or discontinuously, cover or coat the outer surface of the intermediate polymer-coated substrate particles. In alternative embodiments, the second water-absorbing polymer may be applied in an amount so as to substantially coat or cover the outer surface of the intermediate polymer-coated substrate.

In certain embodiments, the second water-absorbing polymer may be applied in an amount of at least about 0.01 wt. % water-absorbing polymer relative to the weight of the substrate, at least about 0.1 wt. %, at least about 0.25 wt. %, at least about 0.5 wt. %, at least about 1 wt. %, at least about 1.5 wt. %, or at least about 2 wt. %; and/or less than about 10 wt. %, less than about 7.5 wt. %, less than about 5 wt. %, or less than about 3 wt. %. As used herein, “wt. % water-absorbing polymer relative to the weight of the substrate” refers to the ratio of the weight of the second water-absorbing polymer to the weight of the substrate, multiplied by 100.

In embodiments, the second water-absorbing polymer may be mixed with the intermediate polymer-coated substrate particles to form polymer-coated substrate particles for a time sufficient to evenly distribute the second water-absorbing polymer amongst the volume of intermediate polymer-coated substrate particles. In certain embodiments, the second water-absorbing polymer may be mixed with the intermediate polymer-coated substrate particles for less than about 5 minutes, less than about 4 minutes, less than about 3 minutes, less than about 2 minutes, or less than about 1 minute.

In certain embodiments, the second water-absorbing polymer applied to the binder-coated substrate particles to form intermediate-coated substrate particles in this step can be present in a liquid, such as an emulsion. In such embodiments, this water-absorbing polymer applied in a liquid can include any or all of the properties of the water-in-oil emulsions discussed above. Further, in such embodiments, the water-absorbing polymer in liquid form can be applied to the binder-coated substrate particles to form intermediate-coated substrate particles in this step in the amount of at least about 0.1 wt. % emulsion relative to the weight of the substrate, at least about 0.2 wt. %, at least about 0.3 wt. %, at least about 0.4 wt. %, at least about 0.5 wt. %, at least about 1 wt. %, at least about 2 wt. %, at least about 2.5 wt. %, at least about 3 wt. %, at least about 4 wt. %, at least about 5 wt. %, or at least about 7.5 wt. %.

As discussed above, the methods described herein can include two separate, distinct applications of a water-absorbing polymer in different forms from one another, such as powdered form and in the form of an emulsion. In certain aspects, it may be desirable to add the water-absorbing polymer in powdered form prior to applying the water-absorbing polymer in the form of an emulsion, since this particular order of application can prevent or reduce the water-absorbing polymer in powdered form from clumping.

Methods for Forming Self-Suspending Proppant Particles: Optional Third Application of Water-Absorbing Polymer

In one or more embodiments, a third application of water-absorbing polymer may be optionally applied to the polymer-coated substrate particles. In such embodiments, this optional application of the water-absorbing polymer can include any or all of the properties and parameters discussed above in applying the water-absorbing polymer to the binder-coated substrate particles to form the intermediate polymer-coated substrate particles. For example, in various embodiments, this third application of water-absorbing polymer can include mixing a water-in-oil emulsion comprising a water-soluble polymer with the polymer-coated substrates in a mixing vessel for 2-3 minutes.

Methods for Forming Self-Suspending Proppant Particles: Drying the Polymer-Coated Substrate

In embodiments, the polymer-coated substrate, with or without the third application of water-absorbing polymer, can be dried in order to form self-suspending proppant particles. In such embodiments, this drying step can remove at least a portion of the liquid with which the water-absorbing polymer was suspended during application of the water-absorbing polymer to the substrate, such as that described above with reference to the formation of intermediate polymer-coated substrate particles or the polymer-coated substrate particles.

In certain embodiments, the polymer-coated substrate can be exposed to mild heat, such as a temperature of at least about 100° F., or at least about 150° F.; and/or less than about 300° F., less than about 250° F., or less than about 225° F. In embodiments, the drying temperature can be about 200° F. or less than about 230° F. Any type of oven or drying system, e.g., fluid bed dryer, can be used to dry the polymer-coated substrate, and a particular system can be chosen by one skilled in the art for a specific purpose. The polymer-coated substrate can be exposed to mild heat for at least about 10 minutes, at least about 20 minutes, or at least about 30 minutes.

In certain embodiments, exposing the polymer-coated substrate particles to the temperature ranges described above can be sufficient to cause cross-linking in at least a portion of the one or more water-absorbing polymers present on the substrate surface. In such embodiments, this method of cross-linking is referred to as thermal cross-linking. Without being bound by any particular theories, it is believed that, when the water-absorbing polymer includes a co-polymer or acrylate monomers and acrylamide monomers, the cross-linking can comprise a covalent cross-link that includes the carboxylate anion on the acrylate monomers covalently bonding to another portion of a water-absorbing polymer, such as an acrylamide monomer. Further, without being bound by any particular theories, it is believed that this thermal cross-linking facilitates the securing of the polymer coating around the substrate particle. In certain embodiments, prior to this thermal cross-linking, one or more of the water-absorbing polymers in the polymer-coated substrate particles is linear.

In certain embodiments, the amount of cross-linking of the water-absorbing polymers can be controlled by the temperature and time of heat exposure. In such embodiments, the polymer-coated substrate particles can be exposed to a temperature of at least about 100° F. (38° C.), or at least about 150° F. (66° C.); and/or less than about 250° F. (121° C.), or less than about 230° F. (110° C.); or a temperature of about 180° F. (82° C.) for a time period of at least about 10 minutes, at least about 20 minutes, or at least about 30 minutes.

In various embodiments, the amount of cross-linking of the water-absorbing polymers can be controlled by the anionic content of the water-absorbing polymers present on the polymer-coated substrate particles. In such embodiments, one or more of the water-absorbing polymers can be about 10 mol % to about 50 mol % anionic, or about 20 mol % to about 50 mol % anionic. In certain embodiments, the water-absorbing polymers present in the self-suspending proppants produced according to the methods described herein may be partially cross-linked (e.g., not full cross-linked). In such embodiments, this partial cross-linking may provide sufficient water swellability and suspension of the proppant while still allowing for the ability to settle out when exposed to a conventional breaker.

In certain embodiments, by controlling the heating temperature, exposure time to the heat, and anionic content of the water-absorbing polymers on the outer polymeric coating, self-suspending proppants are formed that exhibit the desirable suspension properties disclosed herein, including the ability to remain suspending in brackish or salt water conditions, while also being able to settle out when exposed to a conventional breaker, as discussed further below.

In certain embodiments, two distinct applications of a water-absorbing polymer in powdered form and in the form of an emulsion can provide different coating properties to the self-suspending proppant, which can result in advantageous performance of the self-suspending proppants. For example, applying a water-absorbing polymer in an emulsion or other liquid can provide a substantially continuous or continuous coating of the water-absorbing polymer to the surface of the substrate particle, as the emulsion or liquid can evenly coat the substrate particle. Further, in certain embodiments, this substantially continuous coating, when subsequently cross-linked, can form a cross-linked coating on the surface of the substrate particle, effectively locking the substrate particle inside this cross-linked polymeric coating. Additionally, in certain embodiments, the application of the water-absorbing polymer in dried powdered form can increase the water-absorbing polymer content in the self-suspending proppant's polymer coating (relative to a single application of the water-absorbing polymer in an emulsion), which may aid in the suspension ability, including in salt water, while still allowing for polymer coating removal from the substrate using conventional breakers.

In certain embodiments, due to the size of the powdered particles of the powdered form of the water-absorbing polymer relative to the size of the substrate, such as various grades of frac sand, and due to the amount of powdered polymer added in the methods described herein, individual substrates may not be fully coated with powdered polymer particles. Even though the substrates may not be fully coated with the powdered polymer particles in certain embodiments, the self-suspending proppant can also include a coating of a water-absorbing polymer that was applied in an emulsion, which may substantially or entirely coat the outer surface of the substrate particle.

Further, in certain embodiments, utilizing two distinct applications of the water-absorbing polymer where each application includes applying the water-absorbing polymer in a different form (e.g., one application with the water-absorbing polymer in powdered form and another application in an emulsion), allows for the modulation of the amount of the water-absorbing polymer present on the substrate particle in a production efficient manner. For instance, in such embodiments, an application of the water-absorbing polymer in an emulsion form can provide a high localized concentration of water-absorbing polymer to the surface of the substrate particles; however, the amount of water-absorbing polymer that may be applied to the surface of the substrate particles may be limited, as only so much of the emulsion can physically coat onto the substrate particles without falling off. Thus in such embodiments, an application of the water-absorbing polymer in powdered form, in addition to the application of a water-absorbing polymer in an emulsion, can increase the water-absorbing polymer content on the substrate surface (relative to a single application of the water-absorbing polymer in emulsion form), which can result in advantageous self-suspending proppant performance, such as an enhanced salt water tolerance, and/or an enhanced suspension ability. Further, this increase in the water-absorbing polymer content on the substrate surface (relative to a single application of the water-absorbing polymer in emulsion form) can be achieved in a production efficient manner, e.g., utilizing a single vessel and a single drying and/or crosslinking step (e.g., via heat exposure).

Methods for Forming Self-Suspending Proppant Particles: Addition of a Flowing Agent

In various embodiments, once the polymer-coated substrate particles are dried thereby forming the self-suspending proppant particles, a flowing agent may be added to the self-suspending proppant particles to aid in handling and distribution of the self-suspending proppant particles in humid environments. In embodiments, the flowing agent can include fumed silica, sodium aluminosilicate, potassium aluminosilicate, calcium aluminosilicate, synthetic zeolites, natural zeolites, or a combination thereof. In one embodiment, the flowing agent can include a synthetic sodium aluminosilicate zeolite. In certain embodiments, other commercially available flowing agents can be used. A non-limiting list of other commercially available flowing agents includes potassium aluminum silicate, silicon dioxide, calcium silicate, and powdered cellulose.

In embodiments, at least about 0.05 wt. % flowing agent relative to the weight of self-suspending proppant particles can be mixed with or added to the self-suspending proppant particles, at least about 0.1 wt. %, at least about 0.25 wt. %, at least about 0.5 wt. %, at least about 0.75 wt. %, or at least about 1 wt. %, and/or less than about 5 wt. %, less than about 4 wt. %, less than about 3 wt. %, or less than about 2 wt. %. In certain embodiments, about 0.1 wt. % flowing agent relative to the weight of self-suspending proppant particles can be added, about 0.25 wt. %, about 0.5 wt. %, about 0.75 wt. %, about 1 wt. %, about 2 wt. %, about 3 wt. %, about 4 wt. %, or about 5 wt. %.

Self-Suspending Proppant Particles

As discussed above, the self-suspending proppant particles described herein can include a substrate, e.g., sand particle, having an outer polymeric coating. In embodiments, the outer polymeric coating can be discontinuous. As used herein a discontinuous out polymeric coating refers to a polymeric coating on an outer surface of a substrate (that is or is not coated in binder) that covers less than about 80% of the surface, less than about 70%, less than about 60%, less than about 50%, or less than about 25%. In an alternative embodiment, the outer polymeric coating can be a continuous outer coating that covers at least about 50% of the outer surface of the substrate, at least about 60%, at least about 70%, at least about 80%, at least about 90%, at least about 95%, or at least about 99%.

In embodiments, the self-suspending proppant particles made according to the methods described above can include more than one application of a water-absorbing polymer to form the outer polymeric coating. In certain embodiments, as discussed above, the self-suspending proppant particles can include a first water-absorbing polymer that may be applied to a substrate particle, or binder-coated substrate particle, and a second water-absorbing polymer that may be applied to the intermediate polymer-coated substrate particles.

In certain embodiments, the combined amount of the first water-absorbing polymer applied to the binder-coated substrate particles and the second water-absorbing polymer applied to the intermediate polymer-coated substrate particles can provide an outer polymeric coating weight (or coat weight) to the self-suspending proppant particles of at least about 0.5 wt. % coat weight, at least about 1.0 wt. %, at least about 1.5 wt. %, at least about 2.0 wt. %, at least about 2.5 wt. %, or at least about 3.0 wt. %, and/or less than about 7.5 wt. %, less than about 5.0 wt. %, or less than about 4.0 wt. %. As used herein, wt. % coat weight refers to the ratio of the total weight of the water-absorbing polymer applied to substrate, to the weight of the substrate, multiplied by 100.

In certain embodiments, depending on the application of a binder and one or more water-absorbing polymers, the outer polymeric coating of the self-suspending proppant particles can include glycerol, mineral oil, one or more water-absorbing polymers, or a mixture thereof. In such embodiments, the water-absorbing polymers can comprise, consist essentially of, or consist of one or more linear polyacrylamides. In certain embodiments, the one or more linear polyacrylamides can include two linear polyacrylamides having different molecular weights and/or different mol. % anionic charges.

In one or more embodiments, depending on the application of a binder and one or more water-absorbing polymers, the outer polymeric coating of the self-suspending proppant particles can include glycerol, mineral oil, one or more water-absorbing polymers, or a mixture thereof. In such embodiments, the water-absorbing polymers can comprise, consist essentially of, or consist of one or more of polyacrylamides, polyacrylates, or co-polymers of acrylate monomers and acrylamide monomers.

In various embodiments, the first and second water absorbing polymers can be different from one another. For example, in one embodiment, the first and second water absorbing polymers can be different polyacrylamide polymers of different molecular weights. In such an embodiment, the second water-absorbing polymer, e.g., polyacrylamide polymer, may have a higher molecular weight than that of the first water-absorbing polymer, e.g., a polyacrylamide polymer.

In certain embodiments, the first and second water-absorbing polymers can be different types of polymers, or similar types of polymers with different properties. For example, the first and second water-absorbing polymers can be the same types of polymers, e.g., polyacrylamides, but one may be a linear, non-cross-linked polymer, and the other polymer may be cross-linked. In another example, the first and second water-absorbing polymers can be different types of polymers, such as one being a polyacrylamide and the other being a polyacrylate or co-polymer of acrylate and acrylamide.

In embodiments, the ability to vary the types or properties of the water-absorbing polymers applied to the substrate can impart various beneficial properties to the self-suspending proppant particles. For example, in certain embodiments, by using a cross-linked water-absorbing polymer for at least one of the water-absorbing polymers in the outer polymeric coating one can increase the ability for such a self-suspending proppant particle to remain suspending in brackish water conditions that may be found in various wells.

In one embodiment, a self-suspending proppant having a first water-absorbing polymer comprising linear polyacrylamide (which may be applied via a water-in-oil emulsion) and a second water-absorbing polymer comprising a crosslinked polymer, such as crosslinked polyacrylate or a crosslinked co-polymer of acrylamide and acrylate (which may be applied by to the substrate in powdered form) can greatly increase the suspension of the proppant in various types of salt or brackish water.

In another embodiment, a self-suspending proppant having a first water-absorbing polymer comprising a first linear polyacrylamide and a second water-absorbing polymer comprising a second linear polyacrylamide that is different from the first linear polyacrylamide, or is applied to the substrate differently than the first linear polyacrylamide, can greatly increase the suspension of the proppant in various types of salt or brackish water.

In one or more embodiments, the self-suspending proppants made as described herein may remain suspended in a 1000 ppm CaCO₃ aqueous solution for at least 30 minutes, at least 60 minutes, at least 90 minutes, or at least 120 minutes, at room temperature or, alternatively at a temperature of 170° F., after adding the self-suspending proppant particles to the salt solution and shaking to incorporate.

In certain embodiments, a breaker, such as ammonium persulfate or sodium chlorite, may be present at varying levels in a suspension test, such as that described above. The addition of a breaker may be utilized to determine if the proppant will become suspended, or if already suspended, to determine if the suspended proppant can be “broken” (and settle out). In embodiments, the breaker may be present in an amount of from 1-100 pounds per thousand gallons.

In certain embodiments, by varying the types and/or properties of the first and second water-absorbing polymers utilized in forming the self-suspending proppant particles one may be able to tailor a particular type of self-suspending proppant particle for a particular type of water, such as water containing cations, chlorine, iron, or other ionic components.

The concepts discussed herein will be further described in the following examples, which do not limit the scope of various embodiments described in the claims.

EXAMPLES Example 1: Effect of Various Brackish Well Waters on Specific Self-Suspending Proppants

In this Example, various self-suspending proppants were made and analyzed for their ability to remain suspending in various brackish water samples from fracking wells. Each of the proppants tested in this method have been made according to the methods described above. For example, frac sand (40-70 mesh frac sand, unless otherwise noted below) was added to a mixing device, e.g., a kitchen mixer, and 0.20 wt. % glycerol was added and allowed to mix for two to three minutes. Then a water-in-oil emulsion containing a linear polyacrylamide was added and allowed to mix for two to three minutes, followed by the addition of another linear polyacrylamide in powder form, which was mixed in for a period of two to three minutes. The amounts of water-in-oil emulsion and powdered linear polyacrylamide that were added in the various samples are provided below in Table 1. The proppants were then dried at about 230° F. for 15-20 minutes in an electric frying pan.

TABLE 1 Water-absorbing polymers components in self-suspending proppant samples Amount of Water- Powdered absorbing polyacrylamide polymer Amount of (Hyperfloc ® AF coat weight emulsion 308 product) Sample (wt. %)* Emulsion (wt. %) (wt. %) A 1.5 Hyperfloc ® 3.33 0.5 AE 873H B 2.0 Hyperfloc ® 3.33 1.0 AE 853H C 2.5 Hyperfloc ® 3.33 1.5 (30-50 mesh AE 853H frac sand) D 2.0 Hyperfloc ® 3.33 1.16 AE 852H E 1.5 Hyperfloc ® 2.0 0.5 AE 859H F 1.5 Hyperfloc ® 3.33 0.66 AE 872H *wt. % of coat weight refers to the ratio of the weight of the water absorbing polymer added (from both the emulsion and the powdered polyacrylamide) to the weight of the frac sand, multiplied by 100. The weight of water absorbing polymer from the emulsion was determined based on the weight percent of polyacrylamide in the emulsion. The emulsion and powdered polyacrylamide were obtained from SNF.

11.88 grams of each of the self-suspending proppants were added to 45 mL of various test waters in a 50 mL tube (2.2 ppg), capped, and then shaken by hand vigorously for thirty seconds. The shaken tubes were observed over time the settling of the self-suspending proppants. The results appear below in Tables 2-4.

TABLE 2 Suspension results in brackish well water sample #1 Well water sample #1: 11.73 mS conductivity and pH of 8.34 First Second Third Fourth Fifth reading: reading: reading: reading: reading: Time and Time and Time and Time and Time and Suspension Suspension Suspension Suspension Suspension Sample Level* Level* Level* Level* Level* A 0 min. - 100% 5 min. - 18 min. - 60 min. - 120 min. - (6 mL) 37 mL 42 mL 43 mL 44 mL B 0 min. - 100% 5 min. - 10 min. - 47 min. - 107 min. - (6 mL) 22 mL 25 mL 27 mL 28 mL C 0 min. - 100% 58 min. - n/a n/a n/a (6 mL) 28 mL D 0 min. - 100% 5 min. - 10 min. - 42 min. - 102 min. - (6 mL) 20 mL 25 mL 28 mL 33.5 mL E 0 min. - 100% 5 min. - 37 min. - 97 min. - n/a (6 mL) 31 mL 34 mL 35 mL F 0 min. - 100% 32 min. - 92 min. - n/a n/a (6 mL) 45 mL 46 mL *Suspension level was visually determined based on the position of the top of the suspended proppants in the brackish well water sample #1. For example, 100% suspended refers to seeing no settled proppant and the position of the top of the suspended proppants is approximately at the 6 mL level, as determined based on the graduations on the tube. 28 mL is determined to be 50% suspended.

TABLE 3 Suspension results in brackish well water sample #2 Well water sample #2: 1024 μS conductivity and pH of 7.83 First Second Third Fourth reading: reading: reading: reading: Time and Time and Time and Time and Suspension Suspension Suspension Suspension Sample Level* Level* Level* Level* A 0 min. - 100% 44 min. - 18 min. - 60 min. - (6 mL) 10 mL 42 mL 43 mL B 0 min. - 100% 5 min. - 49 min. - n/a (6 mL) 6 mL 7 mL C 0 min. - 100% 7 min. - 63 min. - n/a (6 mL) 1 mL 15 mL D 0 min. - 100% 5 min. - 53 min. - n/a (6 mL) 6 mL 7 mL E 0 min. - 100% 5 min. - 12 min. - 60 min. - (6 mL) 8 mL 11 mL 28 mL F 0 min. - 100% 4 min. - 11 min. - 64 min. - (6 mL) 30 mL 33 mL 41 mL *Suspension level was visually determined based on the position of the top of the suspended proppants in the brackish well water sample #2. For example, 100% suspended refers to seeing no settled proppant and the position of the top of the suspended proppants is approximately at the 6 mL level, as determined based on the graduations on the tube. 28 mL is determined to be 50% suspended.

TABLE 4 Suspension results in brackish well water sample #3 Well water sample #2: 3.62 mS conductivity and pH of 8.27 First Second Third Fourth reading: reading: reading: reading: Time and Time and Time and Time and Suspension Suspension Suspension Suspension Sample Level* Level* Level* Level* C 0 min. - 100% 3 min. - 24 min. - 92 min. - (6 mL) 21 mL 21 mL 26 mL *Suspension level was visually determined based on the position of the top of the suspended proppants in the brackish well water sample #3. For example, 100% suspended refers to seeing no settled proppant and the position of the top of the suspended proppants is approximately at the 6 mL level, as determined based on the graduations on the tube. 28 mL is determined to be 50% suspended.

TABLE 5 Suspension results in fresh water sample Fresh water sample: 2.43 mS conductivity and pH of 8.05 First reading: Second reading: Third reading: Time and Time and Time and Suspension Suspension Suspension Sample Level* Level* Level* C 0 min. - 100% 21 min. - 90 min. - (6 mL) 16 mL 24 mL *Suspension level was visually determined based on the position of the top of the suspended proppants in the fresh water sample. For example, 100% suspended refers to seeing no settled proppant and the position of the top of the suspended proppants is approximately at the 6 mL level, as determined based on the graduations on the tube. 28 mL is determined to be 50% suspended.

As can be seen in the above results, Samples B and C, which included the same water-absorbing polymers, just with varying coat weight, unexpectedly appeared suspended longer than the other samples (aside from Sample D). For example in brackish water samples #1 and #2, at least 50% of Sample B and C were suspended after about one hour subsequent to shaking. Further, Sample C performed equally as well in brackish water sample #3 and the fresh water sample. In any of the four water samples tested, Sample C was not observed to be less than 50% suspended within the observed timeframe. Although Sample D stayed almost 100% suspended in brackish water sample #2 about 60 minutes after shaking, the same sample was observed to be less than 50% suspended in brackish water sample #1 after about 102 minutes.

Example 2: Self-Suspending Proppants in 1000 ppm CaCO₃

In this Example, the suspension of various self-suspending proppants were analyzed in 1000 ppm CaCO₃. In this Example two main samples were utilized, a self-suspending proppant having a cross-linked water-absorbing polymer and another self-suspending proppant with only linear water-absorbing polymers. The self-suspending proppant having only linear water-absorbing polymers was made as described in Example 1 with reference to Sample B.

For the self-suspending proppant having a cross-linked water-absorbing polymer, frac sand (40-70 mesh) was added to a mixing device, a kitchen mixer, and 0.26 wt. % glycerol was added and allowed to mix for less than two minutes. Then 0.45 wt. % SNF Hyperfloc® AE 873H linear polyacrylamide emulsion was added and allowed to mix for two to three minutes, followed by the addition of 2 wt. % of an acrylamide and potassium acrylate co-polymer, cross-linked (Evonik Industries Stockosorb® S 18G) in powder form, which was mixed in over a period of about five minutes. Next an additional 0.45 wt. % SNF Hyperfloc® AE 873H linear polyacrylamide emulsion was added and allowed to mix for two to three minutes. The proppants were then dried at 200° F. for 30 minutes in a conventional oven and 0.5 wt. % fumed silica was added.

Approximately the same amount of proppants were added to separate vials containing a 1000 ppm CaCO₃ solution and shaken vigorously for thirty seconds and allowed to sit in an oven at a temperature of 170° F. for 75 minutes. An additional vial contained the linear polyacrylamide self-suspending proppant and the same 1000 ppm CaCO₃ solution along with a breaker and was treated similarly. After 75 minutes at 170° F., both self-suspending proppants remained suspended in the brackish conditions. In addition, the vial containing the linear polyacrylamide self-suspending proppant and the breaker settled out, suggesting that such an outer polymeric coating can be “broken” with a breaker to settle out the proppant. The cross-linked self-suspending proppant was not exposed to the breaker.

Example 3: Effects of Various Flowing Agents on Self-Suspending Proppants in Humid Conditions

In this Example, various flowing agents were tested with a self-suspending proppant in humid conditions to test for flowability and water absorption. Table 6 below lists the various self-suspending proppant samples and the various flow treatments.

TABLE 6 Flowability Test Proppant Samples Base Sand Coating Flow Agent Mix sand Sample (mesh) Mixture Drying Profile Flow Agent (wt. %) (wt. %) A 30/50 A-1.5% 220° F.-15 min None — 40/70-10% B 30/50 A-1.5% 220° F.-15 min E-554 0.50% — C 40/70 A-1.5% 220° F.-15 min DFC 0.17% — D 40/70 A-1.5% None E-554 0.50% — E 40/70 A-1.5% 220° F.-15 min Whey 1.00% — F 30/50 A-1.5% 220° F.-15 min WPC 34 1.00% — G 30/50 A-1.5% None Whey 1.00% — H 40/70 A-1.5% None WPC 34 1.00% — I 40/70 A-1.5% None E-554 1.00% — J 40/70 A-1.5% None E-554 2.00% — K 30/50 A-1.5% 220° F.-15 min None — — L 30/50 A-1.5% 220° F.-15 min E-554 1.00% — M 40/70 A-1.5% 220° F.-15 min DFC 0.12% — N 40/70 A-1.5% 220° F.-15 min Whey 1.50% — O 40/70 A-1.5% 220° F.-15 min WPC 34 1.50% — P 40/70 A-1.5% 220° F.-15 min F 0.10% — Q 40/70 A-1.5% 220° F.-15 min F 0.15% — R 40/70 A-1.5% None None — —

The proppant samples listed in Table 6 were prepared as described above with respect to sample A of Table 1 in Example 1 to give a coated sand with a 1.5% by weight outer polymeric coating. The same polyacrylamides utilized in sample A of Table 1 in Example 1 were utilized. However, the drying protocol differed as described in Table 6, for example some of the samples were dried with a standard temperature profile, while some were not heat treated. Some of the samples were treated with a flow agent product, as listed in Table 6. Some of the samples were mixed with uncoated sand. The “E-554 (Zeolex 23A)” flow agent is Aerosil R202 fumed silica purchased from Evonik Corporation. The “WPC 34” is a whey protein concentrate at 34% that is commercially available. The “whey” is commercially available. DFC is a proprietary coating utilized to provide a dust-free frac sand.

First, the various proppant samples were exposed to a humidity chamber. Specifically, the samples prepared as in Table 6 were added to an open vial and weighed. Then, the vials were exposed to 85% relative humidity at 90° F. for 15 minutes and weighed thereafter. The temperature and humidity were verified by sensor recordings. The results are listed in Table 7 below.

TABLE 7 Humidity Testing in vials Weight when Pre-Trial Post-Trial Trial Weight Sample prepared (g) Weight (g) Weight (g) Gain (g) A 41.23 41.23 41.24 0.01 B 42.94 42.93 42.95 0.02 C 39.52 39.52 39.53 0.01 D 35.82 35.81 35.81 0 E 41.95 41.94 41.95 0.01 F 42.3 42.29 42.31 0.02 G 31.91 31.92 31.92 0 H 30.56 30.57 30.56 −0.01 I 36.74 36.74 36.74 0 J 39.63 39.62 39.63 0.01 K 40.65 40.65 40.65 0 L 41.05 41.04 41.06 0.02 M 43.13 43.11 43.11 0 N 41.61 41.6 41.62 0.02 O 39.02 39.02 39.04 0.02 P 38.01 38.02 38.02 0 Q 37.88 37.88 37.9 0.02 R 29.95 29.9 29.9 0

Next, the samples exposed to the humidity chamber as above were tested for their ability to flow out of a vial. Specifically, each sample vial was emptied into the Petri dish. The number of shakes/taps of the upside-down vial required to empty the sand from the vial to the Petri dish were recorded. Each time further agitation is required to break up vial sand clumps add 25 shakes/taps to the count. If the equivalent of 100 or more shakes are required, record 100 shakes/taps and empty the remaining contents into the Petri Dish by any means. If a surface clump was formed on the top exposed surface of the vial, record the relative size of the surface clump. The level of bulk clumping visible in each sample, and whether the sand of the sample is uniformly sticking together was recorded. The results appear in Table 8 below and FIG. 12 shows the images of the petri dishes.

TABLE 8 Flow testing from vials Shake/Tap Surface Sample Scale Clump Bulk Sticky A 5 Medium B 5 Medium C 10 Medium Small D 1 Small E 5 Medium F 2 G 100 Bulk Large Yes H 75 Bulk Large Yes I 0 J 0 K 3 Small Small L 1 M 0 Small N 2 Large O 8 Large Small P 1 Small Q 1 Small R 100 Bulk Large Yes

Next the petri dishes from FIG. 12 containing the samples A-R, were subjected to the humidity chamber again, this time for 60 minutes at 90° F. with 85% relative humidity. The temperature and humidity were verified by sensor recordings. The petri dishes were weighed before and after this humidity chamber exposure. The results are listed in Table 9 below.

TABLE 9 Humidity testing in petri dish Pre-Trial Post-Trial Trial Weight Sample Weight (g) Weight (g) Gain (g) A 40.62 40.88 0.26 B 42.29 42.55 0.26 C 38.87 39.1 0.23 D 35.12 35.17 0.05 E 41.36 41.65 0.29 F 41.64 41.93 0.29 G 31.18 31.22 0.04 H 29.91 29.92 0.01 I 36.04 36.1 0.06 J 38.93 38.99 0.06 K 39.97 40.16 0.19 L 40.23 40.51 0.28 M 42.22 42.49 0.27 N 40.84 41.13 0.29 O 38.4 38.66 0.26 P 37.28 37.52 0.24 Q 37.07 37.31 0.24 R 28.55 28.52 −0.03

The samples in the petri dish were dumped over onto white pieces of paper and are shown in FIG. 13 .

Next the samples on the white pieces of paper were evaluated for flowability by being transferred back to their original vials using a plastic funnel. Specifically, an empty funnel was placed into the sample's original sample vial and the sand sample was slid off the paper into the sample funnel. The funnel was shaken vertically 15 times to break up the sand sample in an attempt to have the sand gravity flow into the sample vial. If the humidified sand sample formed a Petri dished shaped clump when slid into the funnel, it was noted how easily the clump breaks up when during the shaking. Further, it was noted how easily the sample sand flowed into the vial from the funnel once the initial clump was broken up (if present). The approximate fill volume of sample sand that was returned to each of the original sample vials was recorded. The overall flow and transfer of humid sand was scored according to the following Table 10 and the results are listed in Table 11.

TABLE 10 Scoring for the flow transfer return to vials Points Scored Clump Breakage Funnel Flow Vial Fill 20 No Clump 15 Very Easy Very Easy 90-110%  10 Easy Easy 75-90% 5 Slightly Difficult Slightly Difficult 50-75% 2 Difficult Difficult 25-50% 1 Very Difficult Very Difficult   <25% 0 No Breakage No Flow    0%

TABLE 11 Flow transfer return from vials Funnel Loading Sample Clump Breakage Flow Vial Fill Score I No Clump Very easy 90-110%   50 J No Clump Very easy 90-110%   50 D No Clump Easy 90-110%   45 B Very Easy Easy 90-110%   40 L Very Easy Easy 90-110%   40 P Very Easy Easy 90-110%   40 Q Very Easy Easy 90-110%   40 K Easy Difficult 50-75%  17 O Slightly Difficult Difficult 50-75%  12 A Difficult Difficult <25% 5 E Difficult Difficult <25% 5 F Difficult Difficult <25% 5 M Difficult Difficult <25% 5 N Difficult Difficult <25% 5 C Very Difficult Very Difficult <25% 3 G Very Difficult Very Difficult <25% 3 H Very Difficult Very Difficult <25% 3 R Very Difficult Very Difficult <25% 3

Based on the above results from Tables 7-11 a humidity and flow correlation analysis was performed, which is shown in Table 12.

TABLE 12 Mixture variation performance analysis Drying Profile 220° F.-15 min None Flow Weight Tap Flow Weight Tap Score Gain Scale Score Gain Scale Flow Agents AVG AVG AVG AVG AVG AVG E-554 40.0 0.79% 3 48.3 0.19% 0 Sample B 40.0 0.74% 5 Sample D 45.0 0.18% 1 Sample I 50.0 0.21% 0 Sample J 50.0 0.19% 0 Sample L 40.0 0.84% 1 F 40.0 0.80% 1 Sample P 40.0 0.79% 1 Sample Q 40.0 0.80% 1 None 11.0 0.67% 4 3.0 −0.14% 100 Sample A 5.0 0.77% 5 Sample K 17.0 0.58% 3 Sample R 3.0 −0.14% 100 WPC 34 8.5 0.83% 5 3.0 0.04% 75 Sample F 5.0 0.84% 2 Sample H 3.0 0.04% 75 Sample O 12.0 0.83% 8 Whey 5.0 0.85% 4 3.0 0.17% 100 Sample E 5.0 0.84% 5 Sample G 3.0 0.17% 100 Sample N 5.0 0.86% 2 DFC 4.0 0.74% 5 Sample C 3.0 0.72% 10 Sample M 5.0 0.77% 0 Grand Total 18.1 0.78% 4 25.7 0.11% 46

Next various samples were subjected to centrifugal settling. The proppant samples are listed below in Table 13. The samples were made as discussed above with respect to the samples in Table 6.

TABLE 13 Proppant samples for centrifugal compression Flow Agent Added (% by weight) Sample ID Base Preparation E-554 - sodium aluminosilicate W 40/70, A-1.5% coat 0.5% weight, Undried X 40/70, A-1.5% coat 1.0% weight, Undried V 40/70, A-1.5% coat 2.0% weight, Undried

For each of the above samples, a 2.1 g standard method sample was prepared of 40/70 mesh dried sand coated with the standard polymer mixture, dried using the standard temperature profile, and 0.1% weight percent of Product F (fumed silica) added.

2.1 g of each of samples W, X, and V (and the standard samples) was hydrated, by placing it in 8 ml of water inside its own 15 ml centrifuge tube. Each tube was then shaken vigorously to mix the proppant and water mixture and then centrifuged at a low speed for 2-5 minutes. A speed a 13% was used for this testing. The centrifuge was an IEC International Centrifuge Model HT. This centrifuge did not have working instrumentation to show its rotational speed. According to associated literature, the model centrifuge should have a maximum speed of 17,000 RPM and generate a relative centrifugal force of 34375. After spinning at 20% speed the rotor RPM was tested with a separate instrument which gave a value of 3300 RPM. This is consistent with a maximum 100% speed of 17,000 RPM. After centrifuging, the samples were removed and the settling of the materials was compared.

No difference in settling was noted in the samples spun for 5 minutes. The Sample X spun for 3 minutes showed slightly less settling than the standard method sample. The undried samples with the sodium aluminosilicate had more opaque gel layer than that of the standard samples.

Finally, another centrifugal compression test was performed. The samples for this test were prepared according to the below Table 14.

TABLE 14 Centrifuge compression samples Flow Base Sand Coating Drying Flow Agent Taps to Sample (mesh) Mixture Profile Agent Amount Mix Sand Remove B 30/50 A-1.5% 220° F.-15 min E-554 0.50% 1 I 40/70 A-1.5% None E-554 1.00% 9 K 30/50 A-1.5% 220° F.-15 min None 40/70-20% 0 Q 40/70 A-1.5% 220° F.-15 min F 0.15% 3

The samples were prepared as indicated in the Table 14 and according to the procedures set out with respect to Table 6. In this test, 5 ml of each sample proppant was placed into a 15 ml centrifuge tube and centrifuged at a medium or high speed for about 5 minutes (for centrifuge force see the above description with respect to Table 13). The samples were removed and the compaction of the materials was compared. The samples were removed by slowly inverting the centrifuge tube above a white paper. If some compressed sand was stuck in the centrifuge tube, the tube was lightly tapped on the table until the sand was removed. Any required taps are recorded in the above Table 14. FIGS. 13A and 13B show the results of the initial dump (FIG. 13A) and the sand fully removed after tapping (FIG. 13B).

In view of these results of Example 3, the flowing agent that worked the best to promote flowability of the coated sand when exposed to high humidity environments is the sodium aluminosilicate (E-554). Unlike the fumed silica samples, the sodium aluminosilicate-containing samples showed unexpectedly beneficial properties, such as having coated sand product flowability even when added to product that was not heat treated with a drying process.

The amount of water vapor absorbed by the coated sand mixtures was not changed significantly by the flowing agents added. If the coated sand was not heat treated by drying after coating, it didn't absorb as much moisture in the humid environment. When exposed to an environment of 90° F. and 85% relative humidity for 60 minutes the undried samples increased weight an average of 0.1% compared to an average weight increase of 0.8% for the dried samples.

The present invention may be embodied in other specific forms without departing from its spirit or essential characteristics. The described embodiments are to be considered in all respects only as illustrative, and not restrictive. The scope of the invention is, therefore, indicated by the appended claims, rather than by the foregoing description. All changes which come within the meaning and range of equivalency of the claims are to be embraced within their scope. 

What is claimed and desired to be secured by United States Letters Patent is:
 1. A method for producing a self-suspending proppant particle, the method comprising: providing a substrate, constituted as discrete particles; providing a water soluble material as a binder; providing a first composition containing a polymer, and formed as a first powder; coating the substrate individually with the binder; forming granules by coating the binder on the substrate individually with the first powder; providing a second composition containing a flowing agent to increase flowability of the resultant granules, and formed as a second powder; and forming granules by coating the first powder on the substrate individually with the second powder, wherein the self-suspending proppant particles are configured to remain suspended in a 1000 ppm CaCO₃ aqueous solution for at least 30 minutes at a temperature of approximately 170° F.
 2. The method of claim 1, wherein the second composition is selected from the group consisting of sodium aluminosilicate, fumed silica, potassium aluminosilicate, calcium aluminosilicate, silicon dioxide, calcium silicate, powdered cellulose, whey protein, and DFC.
 3. The method of claim 1, wherein the second composition is whey protein.
 4. The method of claim 1, wherein the first composition comprises a plurality of polymers, distinct from one another.
 5. The method of claim 3, where in the first composition comprises a plurality of polymers, distinct from one another.
 6. The method of claim 1, wherein the second composition comprises at least two compounds selecting from the group consisting of sodium aluminosilicate, fumed silica, potassium aluminosilicate, calcium aluminosilicate, silicon dioxide, calcium silicate, powdered cellulose, whey protein, and DFC.
 7. The method of claim 1, wherein the second composition consists of whey protein and fumed silica.
 8. The method of claim 1, wherein the second composition consists of whey protein and sodium aluminosilicate.
 9. The method of claim 1, wherein the substrate has a first density and the first powder has a second density, the first density being greater than the second density.
 10. The method of claim 9, wherein the first and second densities are selected, and the size of the granules is selected to effect sinking the polymer, by the substrate, into a fluid.
 11. The method of claim 10, wherein the fluid is moving as a carrier, characterized by a viscosity, and the polymer is selected based on its effectiveness to increase in size by absorbing the fluid.
 12. A method for producing a coated proppant particle, the method comprising: providing a substrate, constituted as discrete particles; providing a water soluble material as a binder; providing a first composition containing a polymer, and formed as a first powder, wherein the substrate has a first density and the first powder has a second density, the first density being greater than the second density; coating the substrate individually with the binder; forming granules by coating the binder on the substrate individually with the first powder; providing a second composition containing a flowing agent to increase flowability of the resultant granules, and formed as a second powder, wherein the second composition is selected from the group consisting of sodium aluminosilicate, fumed silica, potassium aluminosilicate, calcium aluminosilicate, silicon dioxide, calcium silicate, powdered cellulose, whey protein, and DFC; and forming granules by coating the first powder on the substrate individually with the second powder, wherein the coated proppant particles are configured to remain suspended in a 1000 ppm CaCO₃ aqueous solution for at least 30 minutes at a temperature of approximately 170° F.
 13. The method of claim 12, wherein the second composition consists of whey protein and fumed silica.
 14. The method of claim 12, wherein the second composition consists of whey protein and sodium aluminosilicate.
 15. The method of claim 12, wherein the first and second densities are selected, and the size of the granules is selected to effect sinking the polymer, by the substrate, into a fluid.
 16. The method of claim 15, wherein the fluid is moving as a carrier, characterized by a viscosity, and the polymer is selected based on its effectiveness to increase in size by absorbing the fluid.
 17. The method of claim 12, wherein the substrate is a proppant selected from the group consisting of a sand, a ceramic, and a rock product.
 18. A method for producing a coated proppant particle, the method comprising: providing a substrate comprising discrete particles; providing a binder; providing a first composition containing a plurality of polymers, formed as powders and distinct from one another; coating the substrate individually with the binder; forming granules by coating the binder on the substrate individually with the first composition; providing a second composition containing a flowing agent to increase flowability of the resultant granules, and formed as a second powder, wherein the second composition is selected from the group consisting of sodium aluminosilicate, fumed silica, potassium aluminosilicate, calcium aluminosilicate, silicon dioxide, calcium silicate, powdered cellulose, whey protein, and DFC; and forming granules by coating the first powder on the substrate individually with the second powder, wherein the coated proppant particles are configured to remain suspended in a 1000 ppm CaCO3 aqueous solution for at least 30 minutes at a temperature of approximately 170° F.
 19. The method of claim 18, wherein the substrate is a proppant selected from the group consisting of a sand, a ceramic, and a rock product.
 20. The method of claim 19, wherein the second composition comprises a plurality of flowing agents, distinct from one another. 